Pipe Hanger Design & Engineering (April 07)

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Today Anvil® International is the largest and most complete fitting and hanger manufacturer in the world. 2004 Anvil® International acquires Star Pipe Products, Building and Construction TM Divisions (SPF) and forms AnvilStar Fire Products Division. 2001 Anvil® International acquires Merit® Manufacturing and Beck Manufacturing. 2000 The industry’s trusted manufacturer of pipe fittings, hangers and grooved fittings is renamed Anvil® International, Inc.

TRUSTED FOR 150 YEARS

1999 Tyco sells the distribution and manufacturing operations known up to this point as ”Grinnell Supply Sales”, but keeps the Grinnell® trademark.

We built our reputation from the ground up. Anvil’s history stretches back to the mid 1800s, when a company named Grinnell® began providing its customers with the finest quality pipe products. Since 2000, those quality products and services— and the people who provide them—have been known as Anvil® International. Anvil® customers receive the quality and integrity that have been building strong connections in both products and business relationships for over 150 years.

1994 J.B. Smith™ and Catawissa™ join the Grinnell Supply Sales and Manufacturing division.

Focused Product Line: 1969 Grinnell Co. acquired by International Telephone and Telegraph. Two years later, ITT divests the Fire Protection Division, but keeps the manufacturing and sales divisions that will become known as Anvil® International.

Anvil ® Malleable and Cast Iron Fittings

Gruvlok ® Couplings, Fittings and Valves

Anvil ® Hangers, Supports and Struts

SPF TM Malleable and Cast and Ductile Iron Fittings

Beck Welded Pipe Nipples

SPF TM Grooved Fittings and O’Lets

Anvil ® Seamless Pipe Nipples

1960 Gruvlok® line of grooved fittings is introduced.

®

Anvil Steel Pipe Couplings and Small Steel Fittings Merit ® Tee-Lets and Drop Nipples

1919 General Fire Extinguisher Co. becomes Grinnell Co.

1909 Frederick Grinnell opens a foundry in Cranston, RI. Companies express interest in buying its piping products, laying the groundwork for what would become the Grinnell Supply Sales Division. It would be these manufacturing and sales operations that eventually become Anvil® International.

1850 Providence Steam & Gas Pipe Co. is formed, and Frederick Grinnell purchases a controlling interest. Grinnell® is a registered trademark of Grinnell Corporation, a Tyco International Ltd. company.

B U I L D I N G

ANVIL BRANDS:

C O N N E C T I O N S

T H A T

®

L A S T

J.B. Smith Swage Nipples and Bull Plugs Catawissa ® Wing Unions and Check Valves

PIPING and PIPE HANGER DESIGN and ENGINEERING

W EIGHTS

OF

P IPING M ATERIALS

L OAD C ALCULATION P ROBLEM

The material in this booklet has been compiled to furnish pipe hanger engineers with the necessary data and procedures to determine pipe hanger loads and thermal movements of the pipe at each hanger location. The tabulation of weights has been arranged for convenient selection of data that formerly consumed considerable time to develop. In many instances this information was not available for general distribution. This made it necessary to develop average or approximate weights that may be substituted with actual weights whenever practical.

The "Hanger Load Calculation Problem" is typical of the actual steps required in the solution of any pipe hanger installation.

Great care was taken in collecting and printing data in this booklet to assure accuracy throughout. However, no representation or warranty of accuracy of the contents of this booklet is made by Anvil. The only warranties made by Anvil are those contained in sales contracts for design services or products.

CONTENTS .............................................................................. Page Design of Pipe Hangers ................................................................ 4 Determination of Hanger Locations ............................................. 4 Hanger Load Calculations ............................................................ 6 Thermal Movement Calculations ............................................... 11 Selection of the Proper Hangers ................................................ 13 Typical Pipe Support Specification ............................................ 21 Nuclear pipe Hangers .................................................................. 24 Seismic Supports ........................................................................ 24 Supports for Grooved Piping ..................................................... 27 Application Examples ................................................................. 30 Weights of Piping Materials ........................................................ 37 Charts and Tables ........................................................................ 63

Copyright © 2003 Anvil International, North Kingstown, R.I. sales offices and warehouses on back cover

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3

T HE D ESIGN O F P IPE H ANGERS I NTRODUCTION To avoid confusion, it is necessary to define the terms pipe hanger and pipe support and clarify the difference between the two. Pipe hangers are generally considered to be those metal elements which carry the weight from above with the supporting members being mainly in tension. Pipe supports are considered to be those elements which carry the weight from below with the supporting members being mainly in compression. It has become widely recognized that the selection and design of pipe hangers is an important part of the engineering study of any modern steam generating or process installation. Problems of pipe design for high temperature, high pressure installations have become critical to a point where it is imperative that such aspects of design as the effect of concentrated hanger loads on building structure, pipe weight loads on equipment connections, and physical clearances of the hanger components with piping and structure be taken into account at the early design stages of a project. Engineers specializing in the design of pipe hangers have established efficient methods of performing the work required to arrive at appropriate hanger designs. However, the engineer who devotes varying portions of his time to the design of pipe hangers often must gather a considerable amount of reference data peculiar only to the hanger calculations for his current project. It is the purpose of this article to present a compilation of all information necessary for the design of hangers, including a technical section devoted to the listing of piping material, weights, and thermal expansion data. Also, the discussions of the various steps involved in designing supports, presented here in their proper sequence, should serve as a good reference source for the engineer who only occasionally becomes involved in the essentials of hanger design. The first of these steps is that of determining and obtaining the necessary amount of basic information before proceeding with calculations and detailing of the pipe supports. No design is complete unless the engineer has had the opportunity to review the equivalent of the following project data: • The pipe hanger specification, when available (A typical hanger specification is shown on pages 21 and 22). • A complete set of piping drawings. • A complete set of steel and structural drawings including equipment foundation and boiler structure details. • A complete set of drawings showing the location of ventilating ducts, electrical trays, pumps, tanks, etc. • The appropriate piping specifications and data, which will include pipe sizes and composition identification, wall thicknesses, and operating temperatures.

The steps in which the engineer applies this information are: (1) Determine hanger locations. (2) Calculate hanger loads. (3) Determine thermal movement of the piping at each hanger location. (4) Select hanger types: spring assembly, either constant support, variable spring type, rigid assembly, etc. (5) Check clearance between the hanger components and nearby piping, electrical cable trays, conduits, ventilating ducts, and equipment. The final step will not be discussed to any great degree. This aspect of design is governed solely by the requirements and layouts of the individual job. Instead, attention will be devoted to steps 1 to 4, where the scope of good hanger practice can be generally defined for any installation. Recognizing that each new piping design presents many new challenges to the engineer, no attempt is made to state fixed rules and limits applicable to every hanger design. Rather, the intention is to illustrate ideas which will serve as a guide to a simple, practical solution to any pipe support problem.

I NTEGRAL A TTACHMENTS Integral attachments are fabricated so that the attachment is an integral part of the piping component. Examples of integral attachments include ears, shoes, lugs, cylindrical attachments, rings and skirts. Integral attachments are used in conjunction with restraints or braces where multi-axial restraint in a single member is required. Of particular importance is the localized stresses induced into the piping or piping component by the integral attachments. Several methods to determine the local stresses are available including relatively simple hand/ cookbook calculations provided in Welding Research Council (WRC) Bulletins 107, 198, and 297, ASME Code Cases N-318 and N-392, or through a detailed finite element analysis. Section 121 of ASME B31.1 discusses additional considerations for integral attachments.

H ANGER S PANS Support locations are dependent on pipe size, piping configuration, the location of heavy valves and fittings, and the structure that is available for the support of the piping. No firm rules or limits exist which will positively fix the location of each support on a piping system. Instead, the engineer must exercise his own judgement in each case to determine the appropriate hanger location. The suggested maximum spans between hangers listed in table below reflect the practical considerations involved in determining support spacings on straight runs of standard wall pipe. They are normally used for the support spacings of critical systems.

• A copy of the insulation specifications with densities. SPAN BETWEEN SUPPORTS

• Valve and special fittings lists, which will indicate weights. • The movements of all critical equipment connections such as boiler headers, steam drums, turbine connections, etc. • The results of the stress, flexibility and movement calculation performed for critical systems such as Main Steam, High Temperature Reheat, etc.

4

Nom. Pipe Size (In.)

1 11⁄2 2 21⁄2 3 31⁄2 4 5 6 8 10 12 14 16 18 20 24 30

Span Water (Ft.)

7 9 10 11 12 13 14 16 17 19 22 23 25 27 28 30 32 33

Steam, 9 12 13 14 15 16 17 19 21 24 26 30 32 35 37 39 42 44 Gas, Air (Ft.)

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T HE D ESIGN O F P IPE H ANGERS The spans in table are in accordance with MSS Standard Practice SP-69. They do not apply where concentrated weights such as valves or heavy fittings or where changes in direction of the piping system occur between hangers.

three fourths the suggested maximum span shown in the table on the previous page. In considering the vertical section of the pipe on which H-3 and H-4 are shown, it should first be noted that this section of the pipe could be supported by one hanger rather than two as indicated. Two hangers will certainly provide greater stability than will a single hanger. Another deciding factor as to whether one hanger or a multiple hangers should be used is the strength of the supporting steel members of the structure. The use of two hangers will permit the total riser weight to be proportioned to two elevations of the structure, avoiding the concentration of all the riser load at one building elevation.

For concentrated loads, supports should be placed as close as possible to the load in order to minimize bending stresses. Where changes in direction of the piping of any critical system occur between hangers; it is considered good practice to keep the total length of pipe between the supports less than 3⁄4 the full spans in table below. When practical, a hanger should be located immediately adjacent to any change in direction of the piping.

The locations for hangers H-5 and H-6 are governed by the suggested maximum span as well as the position of the concentrated valve weight. Consequently, H-6 has been located adjacent to the valve, and H-5 at a convenient location between the valve and the 12 inch riser.

S AMPLE P ROBLEM In the sample problem (Figure 1) seven supports are shown on the 12 inch line, and two on the 6 inch pipe. Note that the hanger H-1 has been placed adjacent to the valve weight concentration. The proximity of the hanger to the valve is helpful in keeping the load at terminal connection A to a minimum. Also, the bending stresses induced in the pipe by the valve weight are kept to a minimum.

The location of hanger H-7 will be determined by calculation to satisfy the condition that no pipe load is to be applied to terminal connection C. It is obvious that by moving the hanger along the 12 foot section of pipe, the amount of load on connection C will vary. One support location exists where the entire section will be "balanced", and the load at C equal to zero.

The selection of the location for hanger H-2 entails a change in direction of the pipe between two hangers. In order to avoid excessive overhang of the pipe between hangers H-1 and H-2, the length of pipe between these hangers is made less than H-2 " 5'-0

H-1 ck Che e v l Va " 5'-0

A 3'-0 " 1'-0

" 2'-0"

11'-

0"

The calculations to determine the exact location of H-7 are shown in the section entitled "Hanger Load Calculation".

"

'-0"

"

4'-0

5'-0

NOTE:

6

12"

e

Pip

Allowable load at connection A is 500 lbs.

-0"

10' H-3

Allowable load at connection B and C is zero.

5'-0

All bends are 5 diameter bends.

"

All elbows are L.R. Ells. Operating temperature is 1,050°F. All pipe is Sch. 160 A 335 P12.

-0"

40'

"

"

3'-0

H-5 8

" 5'-0

5'-0

" 2'-0

1

H-8

12'-

"

'-0"

5

"

2'-0

0"

To S u

3'-6

it

"

H-9

0"

FIGURE 1 – SAMPLE PROBLEM

12'-

C

Ga Valtve e

'-0"

5'-0

H-7

H-6

H-4

4'-0

"

4'-0

6" P

ipe

"

5'-0

"

45°

"

7'-0

'-0"

5

"

2'-0 e Gat e v l Va

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B

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5

H ANGER L OAD C ALCULATIONS Consider next the 6 inch section of pipe on which H-8 and H-9 are shown. One of the requirements for this hanger problem is that the load at terminal connection B shall be zero. By placing H-9 directly over connection B, we can easily assure that this load will be zero. Also, this hanger location eliminates any bending stresses in the pipe that would be caused by the weight of the valve and vertical pipe at point B. If H-9 could not be located at this point due to structural limitations, it would be desirable to place it as close as possible to the vertical section of pipe to keep the cantilever effect to a minimum. Hanger H-8 is located at a convenient distance between H-9 and the intersection of the 6 inch and 12 inch pipes. In this instance, the location of adequate building structure will determine the hanger position. The methods involved in locating hangers for this problem are typical of those employed by the hanger engineer in the design of pipe supports. Although the individual piping configurations and structure layout will vary in practically every instance, the general methods outlined above will apply for any critical piping system.

H ANGER L OAD C ALCULATIONS The thermal expansion of piping in modern high pressure and temperature installations makes it necessary for the designer to specify flexible supports, thereby requiring considerable thought to the calculation of hanger loads. Turbine and boiler manufacturers are especially concerned about the pipe weight on their equipment and often specify that the loads at pipe connections shall be zero. The hanger designer must be certain that the loads on the equipment connections of a piping system do not exceed the limits specified by the equipment manufacturers. The majority of supports for a high temperature system are of the spring type. The designer must work to a high degree of accuracy in determining the supporting force required at each hanger location to assure balanced support, in order to select the appropriate size and type of spring support.

The first step in the solution of a hanger load problem is to prepare a table of weights. The table for our sample problem (Figure 1) is: TABLE OF WEIGHTS – SAMPLE PROBLEM (FIGURE 1) Insulation Weight Weight Total Used In Description Weight (Ca-Si) Weight Calc. 12" Sch.160 Pipe 160.3 lb./ft. 20.4 lb./ft. 180.7 lb./ft. 375 lb.

61.2 lb.

436.2 lb.

436 lb.

12" 1500 lb. Check Valve

3370 lb.

163.2 lb.

3533.2 lb.

3533 lb.

12" 1500 lb. Gate Valve

4650 lb.

163.2 lb.

4813.2 lb.

4813 lb.

12" 1500 lb. W.N. Flange

843 lb.

30.6 lb.

873.6 lb.

874 lb.

12" 5 Dia. Bend

1258 lb.

160.2 lb.

1418.2 lb.

1418 lb.

45.3 lb./ft. 11.5 lb./ft.

56.8 lb./ft.

56.8 lb./ft.

6" Sch. 160 Pipe 6" Sch. 160 90° L.R. Elbow

53 lb.

17.2 lb.

70.2 lb.

70 lb.

6" Sch. 160 45° Elbow

26 lb.

6.9 lb.

32.9 lb.

33 lb.

6" 1500 lb. Gate Valve

1595 lb.

80.5 lb. 1675.5 lb.

1676 lb.

Draw a free body diagram of the piping between point A and H-2, showing all supporting forces and all valve and pipe weights (Fig. 2). We will consider the loads and supporting forces between A, H-1 and H-2 acting about the axes x-x' and y-y', and apply the three equations: ΣMx-x' = 0 ΣMy-y' = 0 ΣV=0.

We have prepared a sample problem (Figure 1), in which all of the hangers except H-7 have been located. This illustration is limited to as few pipe sections as possible, but incorporates most of the problems encountered in hanger load calculations.

FIGURE 2 – PLAN VIEW Y A

Check Valve

1.5' .5' 1'-0" 1.5'

3,533

H-1 542 5 ft. Radius

B = 3.19'

7'-0"

4'-0"

1.5'

The calculation of loads for hangers involves dividing the system into convenient sections and isolating each section for study. A free body diagram of each section should be drawn to facilitate the calculations for each hanger load. Most of the free body diagrams presented here include as large a section of the piping system as is practical for a simple arithmetical solution to the problem.

1,418

1.81'

The following solution is not intended to illustrate the only acceptable solution. Rather, it shows a composite of various accepted methods which, for the problem under consideration, produce a well balanced system. Of the approaches that could be made to the solution of any problem, there will be one method that will produce the best balanced system. Although the individual loads may vary, the total of all hanger loads would be the same in every case.

180.7 lb./ft.

12" Sch. 160 L.R. Elbow

1,084

X 1.81'

H-2'

B = 3.19' 8'-0"

X'

3'-0" 11'-0"

Y'

6

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H ANGER L OAD C ALCULATIONS Note that the value for H-2 on this section of the piping system represents only a part of the total hanger force at H-2. For clarity, we have labeled this force H-2'. In the calculations for the next section of pipe beginning at H-2, we will call the hanger force at this point H-2".

FIGURE 3 – ELEVATION VIEW H-2'

H-3' 9'-0"

FIGURE 2A– CALCULATING H-2 H-2' + H-2"

2'-0"

H-2

=

5.19'

2'-0"

723

1,418 5 ft. Radius

(F IG . 2),

S TEP II - T AKING

MOMENTS ABOUT AXIS X - X '

H-3" + H-4' = 11,746 lb.

(F IG . 2),

ΣMx-x'= 0, 1.81(1418) + 6.5(542) - 7(H-1) + 9.5(3,533) - 11(A)=0 2,567 + 3,523 + 33,564 = 7(H-1) + 11(A) 39,564 = 7(H-1) + 11(A)

S TEP III - A DDING

FORCES

ΣV = 0,

A + H-1 + H-2' - 3,533 - 542 - 1,418 - 1,084 = 0 A + H-1+ H-2' = 6,577 Ib. Substituting the value H-2', calculated as 1,022 Ib. in Step I, A + H-1 + 1,022 = 6,577 lb. A = 5,555 - H-1

S TEP IV – S OLVING

THE THREE EQUATIONS

(1) H-2' = 1,022

Step I

(2) 39,654 = 7(H-1) + 11(A)

Step II

(3) A = 5,555 - (H-1)

Step III

Since H-3 = H-3' + H-3" and H-3' = 1293 lb. (see Figure 3), H-3=1,293 lb. + 7,228 Ib. = 8,521 Ib.

Substituting for H-1 in Equation 3,

H-4' = (10 ft. + 15 ft.)(18O.7 Ib./ft.) = 4518 Ib.

A = 5,555 Ib - 5,363 Ib. A=192 lb.; which is below the allowable load at A of 500 Ib. Next, consider the section of pipe between H-2 and H-3 to determine the weight distribution, between these two points, of the 4ft. section of pipe and the five diameter bend.

ΣMH-3' =0,

1.81(1,418) +7(723)-9(H-2")=0 H-2"= 848 Ib.

H-2 = H-2' + H-2" = 1,022 lb. + 848 lb. =1,870 Ib.

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H-4'

H-3" = (10 ft. + 30 ft.)(180.7 Ib./ft.) = 7,228 Ib.

39,654 = 7(H-1) + 11(5,555 - H-1) H-1 = 5,363 Ib.

2(723)+7.19(1418)-9(H-3')=0 H-3' =1,293 Ib.

is maintained. It is not recommended, however, to select arbitrary values for these two forces; instead, the load for each hanger should be such that the elevation of the pipe attachment is above the midpoint of the length of pipe supported by the hanger. Thus, the support will be located above the point where one could consider the weight of the pipe column acting, thereby avoiding a condition where the location of the support lends itself to the "tipping" tendency of the pipe when the support is located below this point.

Since there is 10 ft. of vertical pipe above H-3" and 40 ft. of pipe between H-3" and H-4', let H-3" support 10 ft. plus 30 ft. of pipe load:

Solving Equation (2) by subsitituting for A = 5555 - H-1,

ΣMH-2" =0,

10'-0"

MOMENTS ABOUT AXIS Y - Y '

ΣMy-y' = 0, 1.81(1418) + 8(1 084) - 11(H-2') = 0 2,567 + 8,672 = 11(H-2') H-2' = 1,022 Ib.

65'-0"

S TEP 1 - T AKING

40'-0"

B = Radius x .637, or 5 ft. x .637 = 3.185 ft.

In the next free body diagram (Figure 4) consider the 65 ft. vertical section of the piping system to determine the supporting forces for H-3" and H-4'. FIGURE 4 – ELEVATION VIEW It is apparent that the combined forces H-3" and H-4' equals 65 ft. x 180.7 Ib./ft. Further, both H-3" and H-4' could be H-3" any value, provided the relationship

15'-0"

Also, note that we have considered the weight of the 90° bend acting at the center of gravity of the bend. The distance B is determined from the Chart on page 10 which has been drawn for convenience:

Consider the piping between H-4' and H-5 to determine the weight distribution of the 5 diameter bend and the 5 ft. of horizontal pipe: ΣMH-4" = 0 1.81(1,418) + 7.5(904)-10(H-5') = 0 H-5' = 935 Ib. ΣMH-5' = O 2 .5(904)+8.1 9(148)-10(H-4")=0 H-4"=1,387 Ib. H-4 = H-4' + H-4"= 4518 lb. +1,387 lb. = 5,905 Ib.

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7

H ANGER L OAD C ALCULATIONS FIGURE 5

FIGURE 6 – ELEVATION VIEW

FIGURE 7 – PLAN VIEW

H-4"

H-5' 10'-0"

H-3"

10'-0"

Y R1

7.5'

.27'

2.5'

70 (Elbow)

1.81'

12'-0"

30'-0"

5 ft. Radius

14.94' x 56.8 lbs/ft = 849 lbs

1,418

3.78'

16'-0"

15'-0" 10'-0"

H-4'

904

H-8

∑Mx-x''=0

19(70) + 2.66(341) + 5.03(33) - 9(H-8) + 12.78(849) + 20.73(70) - 21R1=0 13,387 = 9(H-8)21 (R1)

∑V=0,

.07'

6.01' x 56.8 lbs/ft = 341 lbs 2.34' 70 .19'

X

H-9 4.81'

R1 + H-8 + H-9 - 2,031- 70 - 341 - 33 - 849 - 70 = 0 R1 + H-8 + H-9 = 3,394 Ib.

Since H-9 has been calculated as 2,258 Ib.

2.66'

.07(33) + 2.34(341) + 4.81(70)+5(2,031) - 5(H-9) = 0 H-9 = 2,258 Ib.

33 (Elbow)

.03'

5'-0"

∑My-y'=0

4'-0"

It is obvious that some portion of the weight of the 6 in. pipe between the 12 in. line and H-8 must be supported by H-5 and H-6. Therefore, before proceeding through H-5 and H-6, calculate this pipe weight load R1, and introduce it into the free body diagram for H-5 and H-6.

5'-0" Y'

X'

1,676 (Valve) 355 (Pipe) 2,031 Total

R1 + H-8 = 3,394 lb. - 2,258 lb. = 1,136 Ib. H-8 = 1,136 lb. - R1 Substituting this value for H-8 in the Equation 13,387= 9(H-8) + 21R1 13,387 = 9(1,136 lb. - R1) + 21(R1) R1 =264 Ib. H-8 = 1,136 - R1= 1136 lb. - 264 Ib = 872 Ib.

8

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H ANGER L OAD C ALCULATIONS FIGURE 8 – ELEVATION VIEW

FIGURE 9

H-5"

E

H-6 15'-0"

5'-0"

.75'

E

218

1.5'

3.25 Ft. x 56.8 = 185

1.5'

218

E=1.09'

.75'

3'-0"

2'-0"'

3.5'

2'-0"'

3.25'

1.5'

1.5' Radius

5'-0"

1,807

4,813

994

R1 = 264

Dimension E is determined from the Chart on page 10. 1⁄2 Weight 12" ELL = 218

For the sample problem, E = .726 x 1.5 ft. = 1.09 ft.

TOTAL = 449

The free body diagram shown in Figure 8 extends from H-5 through the 12 in. 90° elbow. This is intended to illustrate that the weight of the 90° elbow may be considered as supported on a beam which passes through the center of gravity of the elbow and rests on the extensions of the tangents as shown in Figure 9.

Solving for distance X,

In Figure 8,

As a final step, check to ensure that the weight of the entire piping system is equal to the total supporting forces of the hangers plus the pipe weight load to be supported by the equipment connections:

ΣMH-5" = 0, 2(449) + 5(1,807) + 11.5(4,813) - 15(H-6) + 15.75(994) +18.91(218) = 0 H-6 = 5,671 Ib. ΣMH-6 =0,

ΣMC = 0, .54(436) - X(H-7) + 6(1,626) + 10.91(218) = 0 X(H-7)= 12,369 X(3515)= 12,369 X = 3.52 ft.

3.5(4,813) + 10(1,807) + 13(449) - .75(994) - 3.91(218) - 15(H-5") = 0

SUMMARY –– SUPPORT FORCES

H-5"= 2,610 Ib. H-5= H-5'+H-5"= 935 lb. + 2,610 Ib. = 3,545 Ib.

Piping System

Support Forces Plus Terminal Weight (Lbs) Point Loads, Ib

109.5 ft. of 12" Pipe @ 180.7 Ib./ft.

FIGURE 10 – ELEVATION VIEW

19,787

A = 192

4,254

H-1 = 5,363

872

H-2 = 1,870

1,730

H-3 = 8,521

140

H-4 = 5,905

33

H-5 = 3545

(1) 12" 1,500 lb. Check Valve @ 3,533 Ib.

3,533

H-6 = 5,671

(1) 12" 1,500 lb. Gate Valve @ 4,813 lb.

4,813

H-7 = 3,515

(3) 12" 5 Dia. Bends @ 1418 lb. H-7 1.5'

(2) 12" 90° L.R. Ells @ 436 lb. C

X

4.5'

30.45 ft. of 6" Pipe @ 56.8 Ib./ft. (2) 6" 90° L.R. Ells @ 70 lb..

1.5' Radius

(1) 6" 45° Ell @33 lb. .54'

C=.96' 1.09' 1⁄2

Weight of Ell = 218 lbs

4.91'

5.46' 1,626

436 2' x 180.7 lbs./Ft. = 361 lbs. 12" Flange = 874 lbs. Total = 1235 lbs.

(1) 12" 1,500 Ib. WN Flange @ 874 lb.

874

(1) 6" 1,500 lb. Gate Valve @ 1,676 lb.

1,676

Total Weight of Piping System.

H-8 = 872 H-9 = 2,258

37,712 Total = 37,712

The Figure 10 diagram shows a method for arriving at the location of H-7 which will allow zero load on connection C. The value of H-7 is equal to the weight of the piping section: H-7= 218 lb. + 1,626 lb. + 436 lb. + 1,235 Ib. = 3,515 Ib.

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9

H ANGER L OAD C ALCULATIONS CALCULATED ARC DISTANCES FOR BENDS AND WELDING ELBOWS 1.2

D T

1.1

"E" Curve

E 1.0

cg 0.9

θ

E

D & E in Inches for 1" Radius

0.8

R

T

0.7

θ/2 0.6

D

A

0.5

"D" Curve 0.4 0.3

0.2

D = R x [TAN(θ/2) + 2/θ - 2 x CSC(θ)] E = 2 x R x [CSC(θ) 1/θ] T = R x TAN(θ/2)

0.1

0.0 0

10

20

30

40

50

60

70

80

90

100

110

120

130

140

150

160

170

180

160

170

180

ø in Degrees

CENTER OF GRAVITY OF AN ARC 1.0

"A" Curve

0.9

A = [2 x R x SIN(θ/2)] θ B = R x [1 - COS(θ) θ C = R x SIN(θ) θ

0.8

A, B &C in Inches for 1" Radius

0.7

0.6 0.5

0.4

R cg

0.3

θ

B θ/2 0.2

"C" Curve

C

"B" Curve A

0.1

0.0 0

10

20

30

40

50

60

70

80

90

100

110

120

130

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ø in Degrees

10

Anvil International, Piping & Pipe Hanger Design and Engineering

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T HERMAL M OVEMENT C ALCULATIONS T HERMAL M OVEMENTS

S TEP 1 – C HART V ERTICAL M OVEMENTS

The next step in the design of pipe hangers involves the calculation of the thermal movements of the pipe at each hanger location. Based on the amount of vertical movement and the supporting force required, the engineer can most economically select the proper type hanger (i.e. Constant Support, Variable Spring, or Rigid Assembly).

Draw the piping system of Figure 1 and show all known vertical movements of the piping from its cold to hot, or operating, position (see Figure 11). These movements will include those supplied by the equipment manufacturers for the terminal point connections. For the illustrated problem, the following vertical movements are known:

The determination of piping movements to a high degree of accuracy necessitates a highly complicated study of the piping system. The simplified method shown here is one which gives satisfactory approximations of the piping movements.

Point A -- 2 in. up, cold to hot

Whenever differences occur between the approximations and actual movements, the approximation of the movement will always be the greater amount.

H-4 - 0 in., cold to hot

Point B -- 1⁄16 in. up, cold to hot Point C -- 1⁄8 in. down, cold to hot

The operating temperature of the system is given as 1,050°F.

FIGURE 11 – VERTICAL MOVEMENTS H-2 H-1 2" U

P

A 4'-0

D ck Che e v l a V

" 9'-0 -0"

-0"

11'

15' 12"

"

e

Pip

H-3

11'-

0"

-0"

40'

H-7

H-6

H-4 "

5'-0 H-5

12'-

'-0"

13

Gat e Valv e

3'-61

⁄8"

0"

'-0"

2

4'-0

"

6" P

ipe

"

H-9

12'-

F

3'-6

J

H-8

G

" 0'-0

2

0"

C

1⁄8"

4'-0

5'-0 "

Dow

n

"

45° H

'-0"

-0" 9'

10 E

" UP

1⁄16

B

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e Gat e v l a V

Anvil International, Piping & Pipe Hanger Design and Engineering

11

T HERMAL M OVEMENT C ALCULATIONS Referring to the thermal expansion table (page 63), the coefficient of expansion for low-chrome steel at 1,050°F is .0946 in.

FIGURE 13C – SECTION E-J 42'-0" 32'-0" 30'-0"

Calculate the movements at points D and E by multiplying the coefficient of the expansion by the vertical distance of each point from the position of zero movement on the riser D E: 55 ft. x .0946 in./ft. = 5.2 in. up at D

17'-0" 3.5'

H-5

E

H-6

H-7

J .46"

1.89"

20 ft. x .0946 in./ft. = 1.89i n. down at E

1.43"

5

6

f

7

S TEP 2 – S ECTION A-D Make a simple drawing of the piping between two adjacent points of known movement, extending the piping into a single plane as shown for the portion between A and D. FIGURE 12 – SECTION A - D 3.20" 5.20"

1 2

2" A

H-1 4'-0"

D

H-2

∆7 = 3.5/42 x 1.43= 0.12in.

∆f = 30/42 x 1.43 = 1.02in.

∆H-7= 0.12in.+0.46in. =0.58in.down

∆F =1.02in. + 0.46in. = 1.48in. down

∆6 = 17/42 x 1.43 = 0.58in. ∆H-6= 0.58in.+ 0.46in. = 1.04in. down ∆5 = 32/42 x 1.43 = 1.09in. ∆H-5=1.09in.+ 0.46in. = 1.55in. down

S TEP 5

FIGURE 14 – SECTION G-H

Draw the section G-H. The movement at G is equal to the movement at F minus the expansion of the leg G-F:

22'-0" 31'-0"

G 1.10"

∆1 = 4⁄31 x 3.20 = .41in.

F

The vertical movement at H-1 = .41 in. + 2 in. ∆H-1 = 2.41 in. up

FIGURE 15A – SECTION B-H .91"

H-9

The vertical movement at H-2 = 2.27 in. + 2 in. ∆H-2 = 4.27 in. up

The movement at H is equal to the movement of the terminal point B (1⁄16 in. up) plus the expansion of the leg B-H: ∆H = .0625in. up + (9ft. x .0946in./ft) ∆H = 0.91in.up

H AT

H-3

FIG. 13A – MOVEMENT AT H-3

To calculate the vertical movement at H-3, multiply its distance from H-4 by the coefficient of expansion.

Elevation 9'-0"

.0625"

H-3

Since H-9 is located at point H, ∆H-9= ∆H = 0.91in.up

3.78"

∆Y =12/23.1 x 2.01in. = 1.04in. ∆H-8 = 1.10in. - 1.04in. = .06in. down

B 40'-0"

∆H-3 =40 ft. x .0946 in./ft. = 3.78 in.up ∆H-3 = 3.78 in. up

Elevation

1.48"

∆2 = 22⁄31 x 3.20 = 2.27in.

S TEP 3 – M OVEMENT

4'-0"

∆G = 1.48in. down - (4ft. x .0946in./ft) ∆G = 1.10in. down

The vertical movement at any hanger location will be proportional to its distance from the end points:

FIGURE 15B – SECTION G-H 23.1' H-9

H-4 0"

.91" 2.01" 0"

S TEP 4 – S ECTION E-J The next section with two points of known movement is the length E-J. Movement at E was calculated as 1.89 in. down. Movement at J is equal to the movement at the terminal point C (1/8 in. down) plus the amount of expansion of the leg C-J: ∆J = .125in. + (3.5ft. x 0946in./ft) = .46in. down 12

H

12'-0" H-8

{

G 1.10"

y

FIG. 13B – SECTION E-J C 1.25"

3.5'

After calculating the movement at each hanger location it is often helpful, for easy reference when selecting the appropriate type hanger, to make a simple table of hanger movements like the one shown at the right.

J .46"

Anvil International, Piping & Pipe Hanger Design and Engineering

Hanger No. ..... Movement H-1 ............. 2.41" up H-2 ............. 4.27" up H-3 ............. 3.78" up H-4 ............. 0" H-5 ............. 1.55" down H-6 ............. 1.04" down H-7 ............. 0.58" down H-8 ............. 0.06" down H-9 ............. 0.91" up

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S ELECTION

OF THE

P ROPER H ANGER

S ELECTION O F T HE P ROPER H ANGER Selection of the appropriate type hanger for any given application is governed by the individual piping configuration and job requirements. Job specifications covering hanger types, however, are of necessity written in broad terms, and some emphasis is placed on the good judgement of the hanger engineer to ensure a satisfactory, yet economical, system. The type of hanger assemblies are generally classified as follows: (1) Flexible hangers, which include hangers of the constant support and variable spring types. (2) Rigid hangers, such as rod hangers and stanchions. (3) Rollers The location of anchors and restraints is not usually considered a responsibility of the hanger designer. Since it is necessary to determine the location of anchors and restraints before accurate and final stress analysis is possible, they are considered a part of piping design.

F LEXIBLE H ANGERS When a pipe line expands vertically as a result of thermal expansion it is necessary to provide flexible pipe supports which apply supporting force throughout the expansion and contraction cycle of the system. There are two types of Flexible hangers: • Variable Spring • Constant Support. Constant Support hangers provide constant supporting force for piping throughout its full range of vertical expansion and contraction. This is accomplished through the use of a helical coil spring working in conjunction with a bell crank lever in such a way that the spring force times its distance to the lever pivot is always equal to the pipe load times its distance to the lever pivot. FIGURE 16 – CONSTANT SUPPORT HANGER D d F Pivot P

Constant Support Fxd=PxD

Because of its constancy in supporting effect the Constant Support hanger is used where it is desirable to prevent pipe weight load transfer to connected equipment or adjacent hangers. Consequently, they are used generally for the support of critical piping systems. Variable Spring hangers are used to support piping subject to vertical movement where Constant Supports are not required. The inherent characteristic of a Variable Spring is such that its supporting force varies with spring deflection and spring scale. Therefore, vertical expansion of the piping causes a corresponding extension or compression of the spring and will

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cause a change in the actual FIG.17 – VARIABLE HANGER supporting effect of the hanger. The variation in supporting force is equal to the product of the amount of vertical expansion and the spring scale of the hanger. Since the pipe weight is the same during any condition, cold or operating, the variation in supporting force results in pipe weight transfer to equipment and adjacent hangers and consequently additional stresses in the piping system. When Variable Spring hangers are used, the effect of this variation must be considered. Variable Spring hangers are recommended for general use on non-critical piping systems and where vertical movement is of small magnitude on critical systems. Accepted practice is to limit the amount of supporting force variation to 25% for critical system applications on horizontal piping. To illustrate the difference in the effect of using a Variable Spring as compared with a Constant Support hanger, refer to the sample problem shown in Figure 1, page 5. The load for Hanger H-1 was calculated as 5,363 Ib. The vertical movement at H-1 was calculated as 2.41 in. up, from the cold to the hot position of the pipe. If a Variable Spring hanger were used at H-1 , the effect of the variation in supporting force would have to be considered. The amount of variation can be determined by multiplying the spring scale in lbs./in. by the amount of vertical expansion in inches. For example, if the Anvil Figure B-268 Variable Spring hanger were considered, the proper spring size would be number 16 which has a spring scale of 1,500 lbs./in. (For convenience, we have neglected the weight of the pipe clamp, rod and hex nuts. In designing hangers for an actual problem, the weight of components should be added to the calculated load.) The amount of variation is 1,500 Ib/in. x 2.41 in. = 3,615 Ib. Standard practice is to calibrate the hanger in such a way that when the piping is at its hot position the supporting force of the hanger is equal to the FIGURE 18 – CONSTANT SUPPORT HANGER calculated load of the pipe. This means that the maximum variation in supporting force occurs when the piping is at its 2.41" cold position, when stresses added to the piping as a result of variations in supporting forces are less critical. The hot load for the variable spring, then is 5,363 Ib. As the direction of movement from cold to hot is upward, the cold load is 5,363 lb. + 3,615 Ib., or 8,978 Ib. Figure 18 shows the pipe and spring in both the cold and hot condition.

COLD

HOT

5,363lbs 8,978lbs. 2' 4" 5,363lbs 5,363#lbs

Anvil International, Piping & Pipe Hanger Design and Engineering

13

S ELECTION The purpose of the considerations given to the variation in supporting effect is apparent when you recall that the pipe weight does not change throughout its cold to hot cycle, while the supporting force varies. In Figure 18 (hot condition), the supporting force is equal to the pipe weight. However, in the cold condition, the supporting force is 8,978 lb. while the pipe weight is 5,363 Ib. The hanger would exert an unbalanced force on the pipe equal to the amount of variation, or 3,615 Ib. Most of this force would be imposed directly on connection A, where limits are established for the force which may be applied. Further, safe piping design must be based on total pipe stress which includes bending, torsional, shear, longitudinal, and circumferential stresses. The addition of large forces resulting from spring variations can cause stresses which will greatly reduce the factor of safety of the entire spring system. It is possible to reduce the amount of variability by using a variable spring which has a smaller spring scale, as an Anvil Figure 98 (Variable Spring Hanger).

OF THE

P ROPER H ANGER

The hanger type for H-3 may be variable spring type. It is only necessary that the variable spring have a travel capacity which is greater than the calculated pipe movement of 3.78 in. Such a variable spring hanger is the Fig. 98, which has a working travel range of 5 inches. As this assembly is a riser “trapeze” type, two spring units will be used, each supporting one-half the total load of 8,521 Ib, or 4,261 Ib. The appropriate size hanger is a #15 Fig. 98 with a spring scale of 540 Ib. inch. The amount of variation per spring is 3.78 in. x 540 lb./in., or 2,041 Ib. The hot load setting for each hanger is equal to 1⁄2 the calculated load, or 4,261 Ib. As the direction of movement, cold to hot, is upward, the cold load setting will be 4,261 lb. + 2,041 lb. = 6,302 Ib. Figure 19 shows the supporting forces at H-3 and H-4 when the pipe is at its cold and its hot position. The weight of riser clamps, rods, etc., are not included, for convenience. FIGURE 19– HOT VS. COLD CONDITION

The #16 Fig. 98 has a spring scale of 750 Ib/in., one-half that of the B268. The amount of variability would be reduced by one-half, or 2.41 x 750 = 1,808 Ib. However, it should be obvious that even this change in supporting force is too great for the critical location at H-1. The appropriate hanger type for H-1 is a constant support hanger. This hanger would be calibrated to the calculated pipe weight. It would apply a constant supporting force, ensuring complete support of the pipe throughout the piping expansion. That is, its supporting force would be 5,363 lb. when the pipe was at its cold position, and 5,363 lb. also when the pipe was at its hot position. Hanger H-2 has a calculated load of 1,870 Ib. The vertical movement at this location is 4.27in. up, cold to hot. Although the load may be considered slight, the magnitude of the vertical movement is great, and a considerable amount of supporting force change would occur if a variable spring were used. For example, the appropriate size variable spring is a #12 Figure 98 (the 4.27 in. travel is beyond the travel capacity of the Fig. B-268), which has a spring scale of 225 lb. in. The amount of variation equals 4.21 in. x 225 lb. in., or 947 Ib. This variation, expressed as a percentage, is 947 lb./1,870 lb. x 100, or greater than 50%. Unless the hanger engineer were willing to perform some rather elaborate stress calculations to determine the effect of this variation, it would be safer to apply the accepted rule which limits variability to 25% for critical systems, and rule out the selection of a variable spring in favor of the constant support type hanger. The vertical movement of the pipe at H-3 was calculated as 3.78 in. up, and the load as 8,521 Ib. In selecting the spring type for the hanger assembly, it should be recognized that any variation in supporting force will not produce bending stresses in the piping system. As the supporting forces at H-3 and H-4 are concurrent, no bending is produced as a result of spring variation at H-3. Rather, any supporting force variation will merely result in a corresponding load change at the rigid hanger H-4.

14

The design load for H-3 should allow for a calculated cold load of 6,302 lb. x 2 = 12,604 Ib. The load at rigid hanger H-4 is 1,823 lb. cold, 5,905 lb. hot. All hanger components should be designed for the larger load. Variation in supporting forces at hangers H-5, H-6, H-7 and H-9 will produce reactions at connections B and C. As one of the requirements of the problem under study is that weight loads at B and C shall be zero, these hangers must be of the constant support type. Although it holds true that at H-8 any hanger force variation will cause weight loads at B and C, the load and movement at this hanger location are so slight that the spring variation effect can be considered negligible. The load was calculated as 872 Ib, the movement as .06 in. down. The variability of a #8 Fig. B-268 is .06 in. x 150 Ib/in., or 9 Ib. For practical purposes, a 9 lb. change in supporting force could be neglected and a variable spring selected for Hanger H-8. The selection of hanger types for supports H-1 through H-9 in the sample problem illustrates the many considerations which should be given in selecting the appropriate flexible hanger at each support location for any major piping system.

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S ELECTION

OF THE

P ROPER H ANGER

In selecting flexible hanger types the engineer should consider that: • Wherever constant support hangers are used, the supporting force equals the pipe weight throughout its entire expansion cycle, and no pipe weight reactions are imposed at equipment connections and anchors. • Wherever variable spring hangers are used, the engineer must check to assure that the total variation in supporting effect does not result in harmful stresses and forces within the piping system. • Where piping stresses and reactions are known to be close to allowable, the simplest and, in the long run, most economical type of flexible support is obviously the constant support hanger. • Where piping stresses and end reactions are known to be low, variable spring hangers can be used satisfactorily for most non-critical piping support, and for the support of critical systems where vertical movements are of small magnitude.

R IGID H ANGERS Rigid hangers are normally used at locations where no vertical movement of the piping occurs.

This article is not intended to present a short-cut method for the stress analysis of a piping system. In any instance where it is not obvious to an engineer that he is dealing with a noncritical case, the problem should either be reviewed formally from a total stress view-point, or the decision to use a rigid hanger should be changed and a flexible support be utilized. This article is intended to provide the engineer with a simple and quick method of deciding how he can most economically treat vertical thermal movement on a long, horizontal section of a non-critical piping system. Often, the problem can be expressed in the simple terms of whether he will be able to use a rigid hanger rather than a flexible hanger without producing obviously harmful stresses in the system. Consider a simple example, shown in Figure 20, where the hanger engineer is confronted with the problem of how to best treat vertical movement resulting from thermal expansion of the riser. The horizontal sections at both the top and the bottom of the riser are of any hangers H-2, H-3, H-4, etc., should be spring hangers and which will be rigid hangers (vertical restraints in this instance). The solution must satisfy a condition that the bending stress produced by the restraining action of the hanger is no greater than some acceptable amount, say, in this instance, 10,000 psi. FIGURE 20– VERTICAL MOVEMENT OF RISER

The design considerations for a rigid hanger are pipe temperature, for selection of appropriate pipe clamp material, and load, for selection of components suitable for the pipe weights involved.

°F e Pip = 300 0 h 4 emp Sc 6" gT tin era p O H-1

Pipe clamp material is usually carbon steel for temperatures up to 750°F, and alloy steel for temperatures above 750°F. Malleable iron pipe clamps may be used at temperatures up to 450°F. For piping systems of low operating temperature, where vertical expansion is usually not a factor, the rigid hanger assembly components are selected and designed on the basis of calculated or approximated loads. In some instances, however, the rigid hanger is used in a manner where it does more than merely support the pipe weight, but acts as a restraint against vertical piping movements. It is in these cases that the engineer should exercise care in the location of the rigid hanger and the design load he uses in the selection of components. The location and effect of any restraint, guide or anchor on a high temperature and high pressure system is of necessity a function of the stress analyst. The indiscriminate placing of a restraining device on a piping system could alter the piping stresses and end reactions to a serious degree, changing a conservatively designed system into one which exceeds the limits of good design practices. The hanger engineer, though not as well acquainted with the total stress picture of a piping system as is the stress analyst, must usually decide if the problem is of this “critical” nature, or whether the system under study is such that the effect of adding a restraint for convenience will be negligible. The decision is based on the factors of operating temperature, operating pressure, and the configuration of the system. Recognizing that pipe design is based on total pipe stress, one must determine whether the stresses produced by the addition of a rigid hanger, or vertical restraint, are critical.

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40'

H-2 H-3

12' 17'

H-4 17'

For an operating temperature of 300°F, the expansion for carbon steel pipe is .0182in. per foot. ∆ = 40ft. x .0182in./ft. = .728in. down. (see “Thermal Movement Calculations”, page 11.) From the Chart on Page 67 using values of 6 in. pipe and a deflection of 3⁄4 in., read 17.5 ft. This is the minimum distance from the riser where the first rigid hanger may be placed for this problem. If the locations of the hangers are fixed, as they are for this case, then H-2 must be a spring hanger assembly because it is located only 12 ft. from the riser. Therefore, the nearest rigid hanger will be hanger H-3, located 29 ft. from the riser.

Anvil International, Piping & Pipe Hanger Design and Engineering

15

S ELECTION The amount of vertical movement at hanger H-2 will be proportional to its distance between H-3 and the riser, and can be approximated as shown in Figure 21: FIGURE 21– VERTICAL MOVEMENT AT H-2

H-2 .728" H-2 = 17⁄29 X .728" H-2 = .43" Down

17' H-2

29'

P ROPER H ANGER

P ROBLEM Given 10 in. Sch. 40 pipe, and allowable bending stress of 10,000 psi produced by the restraining effect of the hangers, Find: (1) L-1 and L-2 the distances to the nearest rigid hangers H-1 and H-3, see Figure 22.

H-1 H-3

OF THE

(2) The forces which the hangers must apply to the pipe to allow the 1⁄4 in. and 1⁄2 in. deflections resulting FIGURE 23 – PIPE DEFLECTION from the thermal H-2 expansion of the vertical pipe. Solution:

Thus, H-2 would be selected as a variable spring hanger for .43 in. of downward vertical movement, and H-3 would be designed as a rigid hanger. In the above problem the hanger locations were fixed. If this were not the case, and the hangers could be placed at any convenient location subject to usual hanger span limits, then H-2 would be placed at any distance 17.5 ft. or more from the riser. This would satisfy the condition that a maximum bending stress of 10,000 psi would result from the restraining effect of the hanger. If the allowable effect was given as a higher stress, then the hanger could be placed closer to the riser; if lower, the nearest rigid hanger would be placed a greater distance from the riser. If the hanger were located closer to the riser, a greater restraining force would be applied to the pipe by the hanger. As the location is changed to a greater distance from the riser, a lesser force is required. As illustrated in the following sample problem, this force can be an important factor in the design load of the hanger.

FIGURE 22– PROBLEM H-3 1

⁄4" U

p

L-2

16

This force is applied by the pipe hanger H-1, and, therefore, must be included in the design load for H-1. In this instance, where the piping movement is in the downward direction, the force P is added to the pipe weight to be supported by Hanger H-1. If the pipe weight for H-1 were calculated as 2,000 lb., then the design load for the hanger components is 2,000 lb.+2,700 Ib., or 4,700 lb., as shown in Figure 24.

1⁄2"

P

FIGURE 24 - DESIGN LOAD

Pipe Weight = 2,000lbs. + P = 2,700lbs. Total = 4,700lbs

Pipe Weight = 2,000lbs. + P = 2,700lbs. Total = 4,700lbs

The force P which is required at H-3 can be determined from the Chart on page 69. Using values for l0 in. pipe and a 13 ft. span, P is approximately 3,800 Ib. Since this force restrains the upward movement of the pipe, it should be checked against the pipe weight load to assure that the hanger assembly can exert a force equal to the difference of the force P and the pipe weight load.

H-1 L-1

Use the Chart on page 69 to find the value of force P. For a pipe size of 10 in. and a span of 18.5ft., read P as approximately 2,700 Ib.

18.5'

To solve for L-2 refer to the Chart on page 67 and, using values of 1⁄4 in. deflection and 10in. pipe, read L-2 as 13 ft., the distance to the proposed rigid hanger H-3. As discussed for H1 of this problem, hanger H-3 must apply sufficient force to restrain the pipe vertically against the force resulting from the thermal expansion of the vertical piping above H-2.

H-2

0"

From the Chart on page 67 using values of 1⁄2 in. H-1 deflection and 10 in. pipe, read L-1, as 18.5 ft., the distance from the riser to the rigid hanger H-1. Thus, at a P distance of 18.5 ft., the hanger will exert sufficient force to deflect the pipe 1⁄2 in., producing 10,000 psi bending stress. (See Fig. 23).

1

⁄2" D

own

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S ELECTION

OF THE

P ROPER H ANGER

FIGURE 25 - LOAD AT H-3

FIGURE 26 - LOAD AT H-3

FIGURE 28 - P FORCES

P

3,800lbs

H-3

P H-3 3,800lbs

H-2

H-2

To illustrate, assume that the pipe load at H-3 was calculated as 5,000 Ib, The difference between the pipe weight and the force P would equal 5,000 lb. - 3,800 lb. = 1200 lb., as shown in Figure 26.

Pipe Wt. = 5,000lbs. + Force P = 3,800lbs.

H-1

Total = 1,200lbs

The design load used for hanger H-3 should equal 5,000 Ib, or pipe weight only in this instance. Where the vertical movement is in the upward direction, and the force P approaches the pipe weight load, the rigid hanger will tend to unload. This is, as the pipe expands upward the net force applied to the pipe by the hanger becomes less. If the force P becomes greater than the pipe weight at the hanger, the net force on the hanger becomes compressive rather than tensile. When the system has expanded its full amount, the pipe will tend to lift from the hanger, and the supporting effect of the hanger will be zero. If the pipe weight for the sample problem had been calculated as 3,000 lb., then the net force is 3,000 lb. - 3,800 lb., or 8,00 Ib. upward, as shown in Figure 27. The hanger, in this case, would not be considered as a support for the pipe, but a vertical restraint against upward movement, Therefore, either a greater span should be used in order to reduce the force P, or a spring hanger should be used if L-2 is maintained as 13 ft., in Pipe Wt. = 3,000lbs. order to provide support and allow + Force P = 3,800lbs. the piping to move upward at this hanger location. Using the values Total = 800lbs of L-1 and L-2, as determined in the original problem, the forces P at each hanger are as shown in Figure 28.

2,700lbs

2,700lbs

feet by the factor indicated in the Chart below for the specific stress. Correction Factor for Stresses Other Than 10,000 PSI For Bending Multiply Stress (PSI) Of: Length By: 2,000 2.24 3,000 1.83 4,000 1.58 5,000 1.41 6,000 1.29 8,000 1.12 10,000 1.00 12,000 .91 15,000 .82 20,000 .71

FIGURE 27 - LOAD AT H-3

I LLUSTRATIVE E XAMPLE FIGURE 29 - ILLUSTRATIVE EXAMPLE 3" Up

H-1 12'

H-3

H-2 12'

12'

H-4 12'

H-5 12'

4" Sch 40 Pipe

The forces at H-1 and H-3 have been discussed in some detail, but it should also be noted that the design load for H-2 should include these forces as well. For this example, the design load for H-2 equals the pipe weight plus 3,800 lb., minus 2,700 Ib, or design load = pipe weight load + 1,100 Ib. In the preceding problems, the allowable bending stress due to the restraining effect of the hanger was given as 10,000 psi. This allowable stress will, of course, vary with the individual case. Where the stress is other than 10,000 psi, use the Chart on page 67 to read the minimum span, and multiply the span in

Given: 4in. Sch. 40 pipe, ∆= 3in., and 3,000 psi maximum bending stress through the restraining effect of the first rigid hanger. Find: L, the distance from the riser to the first rigid support.

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Anvil International, Piping & Pipe Hanger Design and Engineering

17

S ELECTION From the Chart on page 67 using values of 4 in. pipe and 3 in. deflection, read a span of 29 ft. This span is based on a stress of 10,000 psi, and, to correct for 3,000 psi, refer to the correction factor chart on the previous page. For a stress of 3,000 psi, the correction factor for spans is 1.83. Multiplying 29 ft. by 1.83, the span for 4 in. pipe with 3 in. deflection at 3,000 psi is 29 x 1.83, or 53 ft. Thus, L, the minimum distance to the first rigid hanger, is 53 ft. The first rigid hanger in the above problem will be H-5, located 60 ft. from the riser. The force P required to restrain the piping vertically can be determined from the Chart on page 69 as about 83 lb., using values of 4 in. pipe and a span of 60 ft. The effect of this force will be considered negligible for this problem.

OF THE

P ROPER H ANGER

R OLLERS The pipe attachment and structural attachment of a hanger assembly should be such that they will permit the hanger rod to swing to allow for lateral movement of the piping where horizontal pipe expansion is anticipated. In some instances, where piping expansion is slight and hanger rods are long, the swing permitted by the pivoting of the rod at the upper and lower connections is sufficient, as shown in Figure 31. FIGURE 31 - PIPE EXPANSION

The vertical movements at hanger locations between H-5 and the riser are as shown in Figure 30. FIGURE 30 - VERTICAL MOVEMENTS H-1 12'

H-3

H-2 12'

12'

0°-36'

H-4 12'

8'-0"

H-5 12'

3" ∆H-1 ∆H-2 ∆H-3 ∆H-4

= = = =

48'⁄60'

x 3" x 3" 24'⁄60' x 3" 12'⁄60' x 3" 36'⁄60'

1"

= 2.4" = 1.8" = 1.2" = 0.6"

The above results are based on an approximate but conservative analysis. Whenever the appropriate charts are used, the values listed should assist the engineer in arriving at an economical, safe design for any rigid hanger assembly. The examples described represent situations not frequently encountered in pipe support design, but do point out that the rigid hanger in some instances is more than a simple pipe support, and that good design must allow for all applicable conditions.

Hot

Cold

1"

In other instances the angularity caused by the horizontal piping movements can appreciably effect the position of the piping system, and can cause harmful horizontal forces within the piping system. In Figure 32, note that, because of the large axial piping movement and short hanger rod, the pipe is pulled 3/4 in. off elevation when it expands 6 in. horizontally.

24" 231⁄4"

HOT

2' 0"

COLD

FIGURE 32 - PIPE EXPANSION

6" 3

⁄4"

6"

18

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S ELECTION

OF THE

P ROPER H ANGER

The condition shown in Figure 32 also places a horizontal force component into the piping system. For example, assume a pipe weight of 1000 lb. for the above hanger, as in Figure 33.

FIGURE 35 - PIPE ROLLERS

FIGURE 33 - HORIZONTAL FORCE

H ANGER R OLLER S UPPORTS 1033#

1000#

258#

1000# 1000#

The 258 lb. horizontal force by itself may not be of great consequence, but where there is a series of hangers located on the same long section of pipe, the effect of the total horizontal force can be serious. (See Figure 34) Total horizontal force= 86 + 172 + 258 + 344=860 Ib

B ASE R OLLER S UPPORTS

FIGURE 34 - TOTAL HORIZONTAL FORCE

It should be noted that where rollers are required, the pipe operating temperatures usually are sufficiently high that pipe insulation is used to reduce heat loss and for personnel protection. In these cases a pipe covering protection saddle should be used in conjunction with the rollers to keep the insulation from crushing.

2' 0"

2"

4"

6"

8"

86#

172#

258#

344#

Certainly, for any system subject to horizontal expansion, the rod angularity from the vertical will result in a horizontal force component. The point where this angularity becomes critical cannot be defined for every case, but accepted practice is to limit the swing from the vertical to 4°. Where this angle is greater than 4°, a pipe roller should be considered. Pipe roller supports are of two basic types: those which attach to overhead structure, and those which are placed beneath the pipe as base supports (see Figure 35).

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Where the piping is not insulated, the pipe will rest directly on the roller. This is common practice for the support of long transmission lines where the gas or fluid transported is not of elevated operating temperatures, but where the pipe run is subject to some change in ambient temperature, as from summer to winter variances. For example, a pipe line 300 ft. long subject to ambient changes from 70° F to 110° F expands only .00306 in./ft. from the low to high temperature. Multiplied by 300 ft., however, the total axial expansion is 300 ft. x .00306i n./ft., or .918 in. In instances of this nature, rollers will be used, but the pipe covering protection saddles will not be required. For economy in the support of low pressure, low temperature systems, and long outdoor transmission lines, hanger spans may be based on the allowable total stresses of the pipe and the amount of allowable deflection between supports.

Anvil International, Piping & Pipe Hanger Design and Engineering

19

S ELECTION

FIGURE 36 - DEFLECTIONS

From the Chart on page 64 find the intersection of the Curve 1 in. in 20 ft., and 10 in. nominal pipe size. Read left to find the allowable pipe span of 40 ft. FIGURE 37 - DETERMINATION OF SPAN 20 '

From the Chart on page 65, the bending stress for 10 in. pipe with a support span of 40 ft. is 3,250 psi, which is below the allowable 10,000 psi.

10"

e

Pip

Span = 40 ft . + + +

stress must be considered with other stresses in the piping, such as those due to the pressure of the fluid within the pipe, the bending and torsional stresses resulting from thermal expansion, etc., in order to design the system for total allowable stress. The stresses and deflections indicated in the Charts on pages 64, 65 and 66 are based on a single span of pipe with free ends, and make no allowances for concentrated loads of valves, flanges, etc., between hangers. The stress and deflection values shown in the Charts on pages 64, 65 and 66 are based on a free end beam formula and reflect a conservative analysis of the piping. Actually, the pipe line is a continuous structure partially restrained by the pipe supports, and the true stress and deflection values lie between those calculated for the free end beam and a fully restrained structure. The deflections and bending stress values indicated represent safe values for any schedule pipe from Sch. 10 to XS pipe. For fluids other than water, the bending stress can be found by first finding the added stress caused by water from the Charts on pages 65 and 66 and multiplying by the specific gravity of the fluid. Add this to the stress value of the pipe empty. For lines which are thickly insulated, find the deflection or bending stress resulting from the weight of pipe bare and multiply by a ratio of the weight of pipe per foot plus insulation to the weight of bare pipe per foot.

P ROBLEM : Find: The maximum economical spacing to provide sufficient drainage for an 8 in. water filled line 600 ft. long. The allowable bending stress is 6,000 psi, and the difference in elevations between the ends of the pipe line is 5 ft.

S OLUTION : Maximum Slope =(5 ft. x l2 in./ft.) = 1in./10ft. 600 ft. From the Chart on page 64, find the intersection of the curve 1 in. in 10 ft. and 8 in. pipe, and read left to a span of 43 ft. From the Chart on page 66, for an 8 in. water filled line with a support span of 43 ft., the bending stress is 8,300 psi, which is greater than the allowable 6,000 psi. Therefore, the maximum span should be based on the allowable bending stress of 6,000 psi. Referring to the Chart on page 66, the maximum span for 8 in. pipe and an allowable bending stress of 6000 psi is 37 ft.

A NSWER : Span = 37 ft

P ROBLEM : Find: The maximum spacing and slope for a 6 in. water filled line where the allowable bending stress is 10,000 psi. The difference in the elevations of the ends of the system is not limited. From the Chart on page 66, the maximum span for a 6 in. water filled line with an allowable bending stress of 10,000 psi is 42 ft.

To illustrate the use of the deflection and stress charts, consider the following examples:

On the Chart on page 64 read from the 42 foot span value to the 6in. pipe curve. Interpolating between the slope curves 1 in. in 10 ft. and 1 in. in 5 ft., read the slope 1 in. in 6 ft.

P ROBLEM :

A NSWER :

Find: The maximum economical hanger spacing for a 10 in. non-insulated steam transmission line, 1,200 ft. long, which will provide sufficient drainage with minimum deflection within an allowable bending stress limit of 10,000 psi. The maximum difference in elevations of the ends of the line is 5ft.

20

Maximum Slope = (5 ft. x l2 in./ft.) = 1in./20ft. 1,200ft.

A NSWER :

+ + +

S OLUTION :

1" in

The stresses indicated in the Chart on page 65 and the Chart on page 66 are bending stresses resulting from the weight of the pipe between supports. It should be realized that this

P ROPER H ANGER

SPAN – FEET

In steam lines with long spans the deflection caused by the weight of the pipe may be large enough to cause an accumulation of condensate at the low points of the line. Water lines, unless properly drained, can be damaged by freezing. These conditions can be avoided by erecting the line with a downward pitch in such a manner that succeeding supports are lower than the points of maximum deflection in preceding spans as shown in Figure 36.

OF THE

Span = 42 ft Pipe is sloped at 1 in. in 6 ft. (A difference in elevation of 7 in. between supports.)

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T YPICAL H ANGER S PECIFICATION TYPICAL PIPE HANGER SPECIFICATION 1. SCOPE This specification shall apply for the design and fabrication of all hangers, supports, anchors, and guides. Where piping design is such that exceptions to this specification are necessary, the particular system will be identified, and the exceptions clearly listed through an addendum which will be made a part of the specification.

2. D ESIGN (a) All supports and parts shall conform to the latest requirements of the ASME Code for Pressure Piping B31.1.0, and MSS Standard Practice SP-58, SP-69, SP-89 and SP-90 except as supplemented or modified by the requirements of this specification. (b) Designs generally accepted as exemplifying good engineering practice, using stock or production parts, shall be utilized wherever possible. (c) Accurate weight balance calculations shall be made to determine the required supporting force at each hanger location and the pipe weight load at each equipment connection. (d) Pipe hangers shall be capable of supporting the pipe in all conditions of operation. They shall allow free expansion and contraction of the piping, and prevent excessive stress resulting from transferred weight being introduced into the or connected equipment. (e) Wherever possible, pipe attachments for horizontal piping shall be pipe clamps. (f) For critical high-temperature piping, at hanger locations where the vertical movement of the piping is 1/2 in. or more, or where it is necessary to avoid the transfer of load to adjacent hangers or connected equipment, pipe hangers shall be an approved constant support design, as Anvil Fig. 80-V and Fig.81-H Where transfer of load to adjacent hangers or equipment is not critical, and where the vertical movement of the piping is less than 1 /2 in., variable spring hangers may be used, provided the variation in supporting effect does not exceed 25% of the calculated piping load through its total vertical travel. (g) The total travel for constant support hangers will be equal to actual travel plus 20%. In no case will the difference between actual and total travel be less than 1 in. The constant support hanger will have travel scales on both sides of the support frame to accommodate inspections. (h) Each constant support hanger should be individually calibrated before shipment to support the exact loads specified. The calibration record of each constant support shall be maintained for a period of 20 years to assist the customer in any redesign of the piping system. Witness marks shall be stamped on the Load Adjustment Scale to establish factory calibration reference point.

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(i) In addition to the requirements of ASTM A-125 all alloy springs shall be shot peened and examined by magnetic particle. The spring rate tolerance shall be ±5%. All three critical parameters (free height, spring rate and loaded height) of spring coils must be purchased with a C.M.T.R. and be of domestic manufacture. (j) Constant supports should have a wide range of load adjustability. No less than 10% of this adjustability should be provided either side of the calibrated load for plus or minus field adjustment. Load adjustment scale shall be provided to aid the field in accurate adjustment of loads. Additionally, the constant support should be designed so that the load adjustments can be made without use of special tools and not have an impact on the travel capabilities of the supports. (k) Constant supports shall be furnished with travel stops which shall prevent upward and downward movement of the hanger. The travel stops will be factory installed so that the hanger level is at the “cold” position. The travel stops will be of such design as to permit future re-engagement, even in the event the lever is at a position other than “cold”, without having to make hanger adjustments. (I) For non-critical, low temperature systems, where vertical movements up to 2 in. are anticipated, an approved pre-compressed variable spring design similar to Anvil Fig. B268 may be used. Where the vertical movement is greater than 2 in., a variable spring hanger similar to Anvil Fig. 98 may be used. Where movements are of a small magnitude, spring hangers similar to Anvil Fig. 82 may be used. (m) Each variable spring shall be individually calibrated at the factory and furnished with travel stops. Spring coils must be square to within 1° to insure proper alignment. Each spring coil must be purchased with a C.M.T.R. and be of domestic manufacture. (n) All rigid rod hangers shall provide a means of vertical adjustment after erection. (o) Where the piping system is subject to shock loads, such as seismic disturbances or thrusts imposed by the actuation of safety valves, hanger design shall include provisions for rigid restraints or shock absorbing devices of approved design, such as Anvil Fig. 200 shock and sway suppressor. (p) Selection of vibration control devices shall not be part of the standard hanger contract. If vibration is encountered after the piping system is in operation, appropriate vibration control equipment shall be installed. (q) Hanger rods shall be subject to tensile loading only (see Table III, Page 37). At hanger locations where lateral or axial movement is anticipated, suitable linkage shall be provided to permit swing.

Anvil International, Piping & Pipe Hanger Design and Engineering

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T YPICAL H ANGER S PECIFICATION suppressor valve shall open again to allow free thermal movement of the piping. The suppressor shall have a means of regulating the amount of movement under shock conditions up to the design load for faulted conditions without release of fluid. The suppressor design shall include a fluid bleed system to assure continued free thermal movement after the shock force subsides. The suppressor shall have a hard surfaced, corrosion resistant piston rod supported by a bronze rod bushing. The assembly shall have self-aligning lubricated bushings and shall be designed so that it is capable of exerting the required force in tension and compression, utilizing the distance.

(r) Where horizontal piping movements are greater than 1 ⁄2 in. and where as the hanger rod angularity from the vertical is less than or equal to 4° from the cold to hot position of the pipe, the hanger pipe and structural attachments shall be offset in such manner that the rod is vertical in the hot position. When the hanger rod angularity is greater than 4° from vertical, then structural attachment will be offset so that at no point will the rod angularity exceed 4° from vertical. (s) Hangers shall be spaced in accordance with Tables I and II (Shown below). (t) Where practical, riser piping shall be supported independently of the connected horizontal piping. Pipe support attachments to the riser piping shall be riser clamp lugs. Welded attachments shall be of material comparable to that of the pipe, and designed in accordance with governing codes.

(y) Paint — Variable spring and constant support units will be furnished prime painted. All other material will receive one shop coat of a red chromate primer meeting the requirements of Federal Specification TTP-636. For corrosive conditions, hangers will be galvanized or painted with Garbo-Zinc #11.

(u) Supports, guides, and anchors shall be so designed that excessive heat will not be transmitted to the building steel. The temperature of supporting parts shall be based on a temperature gradient of 100°F per 1 in. distance from the outside surface of the pipe.

3. H ANGER D ESIGN S ERVICE Hangers for piping 21⁄2 in. and larger, and all spring support assemblies, shall be completely engineered.

(v) Hanger components shall not be used for purposes other than for which they were designed. They shall not be used for rigging and erection purposes.

(a) Engineered hanger assemblies shall be detailed on 81⁄2 in. x 11 in. sheets. Each sketch will include a location plan showing the location of the hanger in relation to columns of equipment. Each sketch will include an exact bill of material for the component parts making up each assembly.

(w) Hydraulic Snubbers — The hydraulic units shall have a temperature stable control valve. The valve shall provide a locking and bleed rate velocity that provides for tamper proof settings. The fluid system shall utilize a silicone fluid with proven compatible seals made of approved compounds. The reservoir shall provide a fluid level indicator for exact reading of reservoir fluid level in any snubber orientation.

(b) Each engineered hanger assembly will be individually bundled and tagged as far as practical, ready for installation. Hanger material for piping 2 in. and smaller shall be shipped as loose material, identified by piping system only. A piping drawing marked with approximate hanger locations and types, and hanger sketches showing typical support arrangements will be furnished.

The valve device shall offer a minimum amount of resistance to thermal movement. Any shock force shall cause the suppressor valve to close. With the suppressor valve closed the fluid flow shall essentially stop, thereby causing the unit to resist and absorb the disturbing forces. After the disturbing forces subside the

(c) Hanger inspections shall be performed in accordance with MSS-SP89 (Section 7.7) and ASME B31.1 (Appendix V).

TABLE I MAXIMUM HORIZAONTAL SPACING BETWEEN PIPE SUPPORTS FOR STANDARD WEIGHT STEEL PIPE Nom. Pipe Size (in) ––>

1

/4

1

1 1/2

2

2 1/2

3

3 1/2

Max Span, Water Serv. (ft.) ––>

4

5

6

8

10

12

14

16

18

20

24

7

7

7

9

10

11

12

13

14

16

17

19

22

23

24

27

28

30

32

Max Span, Vapor Serv. (ft.) ––>

8

9

9

12

13

14

15

16

17

19

21

24

26

30

32

35

37

39

42

/2

3

TABLE II MAXIMUM HORIZONTAL SPACING BETWEEN COPPER TUBING SUPPORTS

22

Nom. Pipe Size (in) ––>

1

3

1

Max Span, Water Serv. (ft.) ––>

5

5

6

7

8

Max Span, Vapor Serv. (ft.) ––>

6

7

8

9

10

/2

/4

1 1/4 1 1/2

Anvil International, Piping & Pipe Hanger Design and Engineering

2 1 /2

3

3 1 /2

4

8

9

10

11

12

11

13

14

15

16

2

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F IELD E NGINEERING W ALKDOWNS FIELD ENGINEERING WALKDOWNS Critical piping systems shall be observed visually, as frequently as deemed necessary, and any unusual conditions shall be brought to the attention of the operating company. Only qualified and trained personnel shall be utilized for these observations. Observations shall include determination of interferences with or from other piping or equipment, vibrations, and general condition of the supports, hangers, guides, anchors, supplementary steel, and attachments, etc.

K. Inadequate clearances at guides

Hanger position scale readings of variable and constant support hangers shall be determined periodically. It is recommended that readings be obtained while the piping is in its fully hot position, and if practical, when the system is reasonably cool or cold sometime during the year as permitted by plant operation. Pipe temperature at time of reading hangers shall be recorded.

O. Excessively corroded valves

Variable and constant support hangers, vibration control devices, shock suppressors, dampeners, slide supports and rigid rod hangers shall be maintained in accordance with the limits specified by the manufacturers and designers. Maintenance of these items shall include, but not necessarily be limited to, cleaning, lubrication and corrosion protection.

L. Inadequate safety valve vent clearances at outlet of safety valves M. Any failed or deformed hanger, guide, U-bolt, anchor, snubber, or shock absorber, slide support, dampener, or supporting steel N. Leaks at flanges, valve bonnets and valve stems

P. Defective traps, separators, strainers, silencers, flexible hose, flexible fittings, and water level gage glasses Q. Unacceptable movements in expansion joints The use of photographs can be an important tool in recording piping systems, hangers and supports. These can be stored with the other records and are beneficial for future reference and will establish a system history for future reference. Each plant should maintain and file the following documentation that exists for each unit: A. current piping drawings B. construction isometrics

Pipe location readings and travel scale readings of variable and constant support hangers shall be recorded on permanent log sheets in such a manner that will be simple to interpret. Records of settings of all hangers shall be made before the original commercial operation of the plant and again after startup.

C. pipeline specifications covering material, outside diameter, and wall thickness

After visually observing piping, hangers, and supports, repairs and/or modifications are to be carried out by qualified maintenance personnel for all of the following items:

G. records of any piping system modifications

D. flow diagrams E. support drawings F. support setting charts

A. Excessively corroded hangers and other support components B. Broken springs or any hardware item which is part of the complete hanger or support assembly C. Excessive piping vibration; valve operator shaking or movements D. Piping interferences E. Excessive piping deflection which may require the installation of spring units having a greater travel range F. Pipe sagging which may require hanger adjustment or the reanalysis and redesign of the support system G. Hanger unit riding at either the top or the bottom of the available travel H. Need for adjustment of hanger load carrying capacity I.

Need for adjustments of hanger rods or turnbuckle for compensation of elevation changes

J. Loose or broken anchors

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23

N UCLEAR & S EISMIC A PPLICATIONS NUCLEAR PIPE SUPPORTS Nuclear pipe support design has evolved from a relatively simple design-by-rule approach to a complex design-byanalysis approach. Pipe support design has presented some major challenges for the nuclear power industry. The ASME Boiler and Pressure Vessel Code, Section III, Division 1 , Subsection NF, “Component Supports”, contains very detailed requirements for nuclear pipe supports. The NF Code contains requirements for material design, fabrication and installation, examination, nameplates, stamping, and reports. The principal differences between nuclear and non-nuclear pipe supports lie in the more sophisticated and demanding design, analysis, additional non-destructive examination (NDE), quality assurance, and Code inspection and stamping. However, the type of pipe supports and materials used for nuclear pipe supports are essentially the same as those used for nonnuclear. The design of nuclear pipe supports is dependent upon a piping analysis which provides the appropriate support loading and displacements. The pipe support designer/analyst must be aware of specific assumptions that the piping analyst used in performing the piping analysis. Typical assumptions are: (1) no excessive support mass on pipe; (2) support is provided in directions shown with type support shown; (3) support is sufficiently rigid to permit decoupling of the analysis of the support from the pipe; (4) support allows for essentially unrestricted movement in the unsupported direction.

Nuclear pipe supports are designed to the same loadings that fossil power plants experience, i.e, thermal, deadweight, thermal equipment displacement loadings, and operating loadings, including turbine trip, rapid valve closure, etc. In addition to these normal loadings, nuclear power plants require detailed analysis for seismic loadings on the piping system. This detailed seismic requirement results in the significant difference between the design of nuclear pipe support versus a conventional power plant. The seismic requirement resulted in piping systems which were considerably stiffer when compared to similar systems without seismic requirements. This was the direct result of providing additional lateral and vertical restraints to resist the seismic loadings on the piping system. The additional restraints reduced seismic stresses, but resulted in increased thermal stresses. To minimize this impact, pipe snubbers were utilized in piping systems. Snubbers are devices which are essentially only active during an earthquake or other dynamic event and offer little resistance to the slow pipe movement resulting from thermal growth. Although snubbers have seen limited use in conventional plants, their primary use was in nuclear facilities. Since the use of snubbers requires a significant amount of functional testing and inspection, their use has been considerably reduced. In addition, most nuclear plants have initiated programs to eliminate as many snubbers as possible. Although the use of snubbers should generally be avoided, they may, in certain circumstances, present the most simple and cost effective solution.

SEISMIC SUPPORTS The following is for reference only. Refer to MSS-SP127 for detailed requirements). Seismology and its effect on building structures, components and attachments affect almost every building code and standard. Increasingly, codes and standards are requiring seismic restraints in critical areas. There are several codes and standards across the country that contain entire sections devoted to seismic restraints and bracing. Some of the more common codes are the Uniform Building Code 1991 and the 1991 California Building Standard Code (CAC Title 24, Part II. The progressive CAC Title 24 states in Section 2330 (a): “Every building or structure and every portion thereof, including the nonstructural components, shall be designed and constructed to resist stresses and limit deflections calculated on the basis of dynamic analysis or equivalent static lateral forces analysis …” It continues in Section 2336(a) “Parts and portions of structure and their attachments, permanent nonstructural components and their attachments, and the attachments for permanent equipment supported by a structure shall be designed to resist the total design lateral seismic force, Fp, given by the following formula: Fp=Z x I x Cp x Wp, Where: Fp = Total Design Lateral Seismic Force. Z = Seismic Zone Factor, Numerical Coefficient as shown in Table 23-1 and derived from Seismic Zones Map on Page 26. 24

I = Importance Factor, as shown on Table No. 23-L and derived from Occupancy Categories shown on Table No. 23-K. Cp = Horizontal Force Factor (“… conduit, ductwork and piping …” has a Cp of 0.75 per the CAC Title 24 and a Cp of 0.45 per the 1991 Uniform Building Code). Wp = Weight of Element or Component (Weight of pipe, ductwork and conduit) The following conduit, ductwork and piping do NOT require bracing per CAC Title 24, Part II: Table No. 23-P, note 12. a. Gas piping less than 1 in. diameter. b. Piping in boiler and mechanical equipment rooms less than 1.25 in. inside diameter. c. All piping less than 2.5 in. inside diameter. d. All piping suspended by individual hangers 12 in. or less in length from the top of pipe to the bottom of the support for the hanger. e. All electrical conduit less than 2.5 in. inside diameter. f.

All rectangular air-handling ducts less than 6 sq. ft. in cross-sectional area.

g. All round air handling ducts less than 28 in. in diameter. h. All ducts suspended by hangers 12 in. or less in length from the top of the duct to the bottom of the support for the hanger.

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S EISMIC C ATEGORIES

TABLE 23-K OCCUPANCY CATEGORIES (I) Essential Facilities (Essential facilities are those structures which are necessary for the emergency operations subsequent to a natural disaster.) • Hospitals and other medical facilities having surgery and emergency treatment areas. • Fire, Sheriff and Police Stations • Municipal, county and state government disaster operation and communication centers deemed vital in emergencies. • Tanks of other structures containing, housing or supporting water or other fire-suppression materials or equipment required for the protection of essential or hazardous facilities, or special occupancy structures. • Emergency vehicle shelters and garages. • Standby power-generating equipment for essential facilities. (II) Hazardous Facilities • Structures housing, supporting or containing sufficient quantities of toxic or explosive substances to be dangerous to the safety of general public if released. (III) Special Occupancy Structure • Covered structures whose primary occupancy is public assembly - capacity ≥ 300 persons. • Buildings for schools through secondary or day-care centers - capacity ≥ 250 students. • Buildings for colleges or adult education schools - capacity ≥ 500 students • Medical facilities with 50 or more resident incapacitated patients, not included above. • Jails and detention facilities. • All structures with occupancy ≥ 5,000 persons. • Structures and equipment in power-generating stations and other public utility facilities not included above, and required for continued operation. (IV)

Standard Occupancy Structure • All structures having occupancies or functions not listed above.

TABLE 23-L EARTHQUAKE IMPORTANCE FACTOR (I), BASED ON OCCUPANCY CATEGORY 1991 Uniform CAC Occupancy Category Building Code Title 24 I. Essential Facility

1.25

1.50

II. Hazardous Facilities

1.25

1.50

III. Special Occupancy Structures

1.00

1.15

IV. Standard Occupancy Structures

1.00

1.00

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Zone -->

TABLE 23-I SEISMIC ZONE FACTOR "Z" 1 2A 28

Zone Factor --> 0.075 0.15

0.20

3

4

0.30

0.40

Refer to zone map on the following page for general information purposes, or visit "http://eqhazmaps.usgs.gov" for current seismic zone information.

Anvil International, Piping & Pipe Hanger Design and Engineering

25

S EISMIC C ATEGORIES 130 W

125 W

45 N

120 W

3

115 W

2B

110 W

105 W

90 W

85 W

80 W

75 W

70 W

60 W

45 N

1

0

4 2B

2B

40 N

0

3

3

65 W

2A

3 3

95 W

3 1

40 N

100 W

2A 1

1

1

0

4 4

2A

3

35 N

35 N

2A 3

1

2B

1

3

1

1

4

2A 30 N

2B

2A

2A

1

1

30 N

0 0 0

25 N

110 W

115 W 161 W 23

160 W

159 W

158 W

105 W 157 W

156 W

100 W 155 W

95 W

154 W 23

90 W

25 N

85 W 170

175

180

80 W

75 W

175 170 165 160 155 150 145 140 135 130 70

0 22

22

1

1 2B

2B 21

65

3

21

2B

4

20

20

3

60

Alaska 3

19 50

50

0

55

4

19 100 MIles

Hawaii 18 161 W

160 W

159 W

158 W

157 W

156 W

155 W

55

18 154 W

3

4

Puerto Rico

0

25

50

The maps shown above are for general information purposes, please visit "http://earthquake.usgs.gov/hazmaps/" for current seismic zone information. 1994 Uniform Building Code zone map. Zones are identified by the numbers from 0 to 4. Seismic zone factors are assigned to each zone; Zone 0 = 0, Zone1 = 0.075, Zone 2A = 0.15, Zone 2B = 0.20, Zone 3 = 0.3, and Zone 4 = 0.4. Each zone also has specific structural detailing requirements.

26

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P IPE S UPPORTS F OR G ROOVED P IPING PIPE SUPPORTS — GROOVED PIPING

C OUPLING F LEXIBILITY :

When designing the hangers, supports and anchors for a grooved end pipe system, the piping designer must consider certain unique characteristics of the grooved type coupling in addition to many universal pipe hanger and support design factors. As with any pipe system, the hanger or support system must provide for

The grooved coupling’s capability to allow angular and rotational movement within the coupling joint must be considered when deciding hanger and support locations. Spring hangers and supports providing for movement in more than one plane are often used to allow the pipe system to move without introducing additional stress into the pipe system.

1) the weight of the pipe, couplings, fluid and pipe system components; 2) reduce stresses at pipe joints; and 3) permit required pipe system movement to relieve stress. The following special factors should be considered when designing hangers and supports for a grooved end pipe system.

P IPE H ANGER S PACING :

PIPE HANGER SPACING FOR STRAIGHT RUNS WITHOUT

The following charts show the maximum span between pipe hangers for straight runs of standard weight steel pipe filled with water or other similar fluids.

LINEAR MOVEMENT IS

Nominal Pipe Size Range 3

NOT REQUIRED. Max.Span Between Hangers

⁄4"— 1"

7'

11⁄4" — 2"

10'

21⁄2"— 4"

12'

5"— 8"

14'

10"—12"

16'

14"— 16"

18'

18"— 24"

20'

PIPE HANGER SPACING FOR STRAIGHT RUNS WITHOUT CONCENTRATED LOADS AND WHERE FULL LINEAR MOVEMENT IS REQUIRED Pipe Length in Feet Nominal Pipe Size *Average Hangers per Pipe Length (Evenly Spaced) Range 7' 10' 12' 15' 20' 22' 25' 30' 35' 40' ⁄4"— 1"

1

2

2

2

3

3

4

4

5

6

11⁄4"— 2"

1

2

2

2

3

3

4

4

5

6

1

1

2

2

2

2

2

3

4

4

1

2 ⁄2" – 4"

FIGURE 38 - SAG DUE TO FLEXIBILITY

L1

L2

CONCENTRATED LOADS AND WHERE FULL

Do not use these values where critical span calculations are made or where there are concentrated loads between supports.

3

Figure 38 demonstrates the need for each pipe length in a grooved system to be supported. The sag due to the flexibility of the Gruvlok joint could be eliminated with the proper positioning of hangers on both “L1” and “L2”.

5" – 8"

1

1

1

2

2

2

2

3

3

3

10" – 12"

1

1

1

2

2

2

2

3

3

3

14" – 16"

1

1

1

2

2

2

2

3

3

3

18" – 24"

1

1

1

2

2

2

2

3

3

3

*No pipe length should be left unsupported between any two couplings.

Sag Due to Flexibility

Figure 39 illustrates the effect of pump oscillation on a piping system. A spring hanger should be used to support the pipe section and also respond to the induced vibrations. The couplings in the horizontal run above the riser, should accommodate the deflection without transmitting bending stresses through the pipe system.

FIGURE 39 - PUMP OSCILLATION

Pump Oscillation

P RESSURE T HRUSTS Gruvlok couplings react to the application of system pressure and restrain the pipe ends from separation due to the pressure force. However, the coupling joint may not be in the selfrestraining configuration prior to the application of system pressure. The Gruvlok coupling does not restrain adjacent pipe sections from separation due to pressure forces until the coupling key sections engage the groove walls. Random coupling joint installation will produce installed coupling conditions ranging from pipe ends fully butted to fully separated to the maximum available gap. Thus, only after system pressurization will the self-restraining function of the coupling be in effect. The designer must account for the movement to be encountered when the system is pressurized and the joints are fully separated. Anchor and guide positions must be defined to direct the pipe joint movement such that it is not detrimental to the pipe system. The effect of pressure thrust are shown in the following examples.

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Anvil International, Piping & Pipe Hanger Design and Engineering

27

P IPE S UPPORTS F OR G ROOVED P IPING FIGURE 40 - PRESSURE THRUST System With No Pressure

∆L

System Pressurized

Figure 42 - To restrain this system provide a pressure thrust anchor at “R1” to resist the pressure thrust acting through the tee “D1” at the cap “C”. Provide a hanger at Point “R2”, or a base support at Point “D2” to support the vertical column. If the offsets L1, L2, and L3 are of adequate length to handle expected pipe movements, no additional anchoring is required. Thermal movement of the pipe system should also be considered, and intermediate anchors located as required, to direct the pipe movement so as to prevent introducing bending stresses into the system.

Figure 40 - The coupling joints have been installed butted or partially open. When pressurized the pipe ends in the coupling joints will separate to the maximum amount permitted by the coupling design.

FIGURE 43 - PRESSURE THRUST D

The coupling key sections will make contact with the groove walls and restrain the pipe from further separation. The movement at each coupling joint will add with all other joints and produce ∆L. FIGURE 41 - PRESSURE THRUST

A

VERTICAL COLUMN E

L1 B

∆M-MOVEMENT DUE TO PRESSURE THRUST

SUFFICIENT LENGTH TO OFFSET PRESSURE THRUST

C

HORIZONTAL RUN

VERTICAL COLUMN

L2

Figure 43 - Anchor at “A” to support weight of vertical water column. Use spring hanger at “D” and “E” to allow movement of vertical piping. Anchors at “B” and “C” if offsets at L1and L2 are insufficiently long to handle expected pipe movements.

Figure 41 - In the system shown here, the pipe will move and deflect at the elbow joint due to pressure thrust. The pipe designer must assure himself that the system has the capability of deflecting sufficiently to absorb this movement without introducing additional stresses into the pipe system. In the deflected condition shown, temperature increases would produce further expansion of the pipe system thus increasing the deflection. FIGURE 42 - PRESSURE THRUST

L1 R1

C

R2 D1

FIGURE 44 - LATERAL RESTRAINT System with no pressure partially deflected

System pressurized fully deflected

Figure 44 [Lateral Restraint] - A grooved coupling joint installed in a partially deflected condition between anchor locations will deflect to its fully deflected condition when pressurized. Hangers and supports must be selected with consideration of the hanger’s capability to provide lateral restraint. Light duty hangers, while acceptable in many installations, may deflect against the application of lateral forces and result in “snaking” conditions of the pipe system.

L2

D2

28

L3

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P IPE S UPPORTS F OR G ROOVED P IPING RISER DESIGN: Risers assembled with Gruvlok couplings are generally installed in either of two ways, In the most common method, the pipe ends are butted together within the coupling joint. Note that when installing risers, the gasket is first placed onto the lower pipe and rolled back away from the pipe end prior to positioning the upper pipe. Anchoring of the riser may be done prior to pressurization with the pipe ends butted or while pressurized, when, due to pressure thrust, the pipe ends will be fully separated. An alternative method of riser installation is to place a metal spacer of a predetermined thickness, between the pipe ends when an additional length of pipe is added to the riser stack, The upper pipe length is anchored, the spacer removed and the coupling is then installed, This method creates a predetermined gap at each pipe joint which can be utilized in pipe systems where thermal movement is anticipated and in systems with rigid (threaded, welded, flanged) branch connections where shear forces due to pressure thrust could damage the rigid connections. The following examples illustrate methods of installing commonly encountered riser designs.

R ISERS W ITHOUT B RANCH C ONNECTIONS Install the riser with the pipe ends butted. Locate an anchor at the base of the riser (A) to support the total weight of the pipe, couplings and fluid. Provide pipe guides on every other pipe length, as a minimum, to prevent possible deflection of the pipe line at the coupling joints as the riser expands due to pressure thrust or thermal growth. Note that no intermediate anchors are required.

R ISERS W ITH B RANCH C ONNECTIONS FIGURE 45 RISER WITHOUT BRANCH CONNECTIONS L M

When the system is pressurized the pipe stack will “grow” due to pressure thrust which causes maximum separation of pipe ends within the couplings. The maximum amount of stack A growth can be predetermined (see Linear Movement). In this example the pipe length “L” at the top of the riser must be long enough to permit sufficient deflection (see Angular Movement) to accommodate the total movement “M” from both pressure thrust and thermal gradients.

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Install the riser with the predetermined gap method. Anchor the pipe at or near the base with a pressure thrust anchor “A” capable of supporting the full pressure thrust, weight of pipe and the fluid column. Anchor at “B” with an anchor capable of withstanding full pressure thrust at the top of the riser plus weight of pipe column.

FIGURE 46 RISER WITH BRANCH CONNECTIONS

Place intermediate anchors “C” as shown, between anchors “A” and “B”. Also place intermediate clamps at every other pipe length as a minimum. When this system is pressurized, the pipe movement due to pressure thrust will be restrained and there will be no shear forces acting at the branch connections.

Anvil International, Piping & Pipe Hanger Design and Engineering

B

C

C

C

A

29

E NGINEERED H ANGER A PPLICATIONS

Constant Hanger Assemblies

66 80 V TYPE B

80V TYPE A

140, 146

C-C (NEEDED)

290

140, 146 290

295, 295A, 295H

40

Fig_80V_Type_B .DWG, .DXF, or .EPS

Fig_80V_Type_A .DWG, .DXF, or .EPS

80V TYPE D 55L 291

80V TYPE E

80 V TYPE C

140, 146

140, 146 224, 246

290

290

295, 295A, 295H

295, 295A, 295H

Fig_80V_Type_D .DWG, .DXF, or .EPS

Fig_80V_Type_C .DWG, .DXF, or .EPS

66 290

140, 146

Fig_80V_Type_E .DWG, .DXF, or .EPS

66

66

290

290

140, 146

140, 146

81-H TYPE A

81-H TYPE A

140, 146

C-C (NEEDED) 137 S

80 V TYPE G 160-166A

140, 146

290

290

295, 295A, 295H

224, 246

60 Fig_80V_Type_G .DWG, .DXF, or .EPS

Fig_81H_Type_A_224 .DWG, .DXF, or .EPS

Fig_81H_Type_A_295 .DWG, .DXF, or .EPS

Each of these drawings are available on the Anvil web site in CAD format. The file name at the bottom of each box refers to that CAD file.

30

Anvil International, Piping & Pipe Hanger Design and Engineering

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E NGINEERED H ANGER A PPLICATIONS

Constant Hanger Assemblies (continued)

66

66

55 LUG 291 81-H TYPE C

81-H TYPE B

81-H TYPE B

140, 146 140, 146

140, 146 299

290

53-SD WELD LUG

290

295, 295A, 295H

295, 295A, 295H

ELBOW Fig_81H_Type_B_295 .DWG, .DXF, or .EPS

Fig_81H_Type_B_53_SD .DWG, .DXF, or .EPS

Fig_81H_Type_C .DWG, .DXF, or .EPS

81-H TYPE D

140, 146 299 53-SD WELD LUG

81 H TYPE F ELBOW Fig_81H_Type_D .DWG, .DXF, or .EPS

Fig_81H_Type_F .DWG, .DXF, or .EPS

Each of these drawings are available on the Anvil web site in CAD format. The file name at the bottom of each box refers to that CAD file.

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Anvil International, Piping & Pipe Hanger Design and Engineering

31

E NGINEERED H ANGER A PPLICATIONS

Spring Hanger Assemblies 60

66

66

290 140, 146

290

82, 268, 98 TYPE A

140, 146 290 212, 216

140, 146

140, 146

82, 268, 98 TYPE A

82, 268, 98 TYPE A

140, 146

140, 146

290

290

295, 295A, 295H

295, 295A, 295H

SH_Type_A_212 .DWG, .DXF, or .EPS

SH_Type_A_60 .DWG, .DXF, or .EPS

SH_Type_A_295 .DWG, .DXF, or .EPS

60 140, 146 66 290 140, 146

66 82, 268, 98 TYPE A

290 C-C (NEEDED)

140, 146 82, 268, 98 TYPE A

82, 268, 98 TYPE A 140, 146 140, 146 299 53-SD WELD LUG

299

140, 146

53-SD WELD LUG 290

40 ELBOW SH_Type_A_53SD .DWG, .DXF, or .EPS

66

82, 268, 98 TYPE B

140, 146

290

ELBOW SH_Type_A_53SD_60 .DWG, .DXF, or .EPS

SH_Type_A_Riser.DWG, .DXF, or .EPS

55L

66

291

82, 268, 98 TYPE B

82, 268, 98 TYPE C

140, 146 299

140, 146 290

53-SD WELD LUG

295, 295A, 295H

212, 216

ELBOW SH_Type_B_295 .DWG, .DXF, or .EPS

SH_Type_B_53SD .DWG, .DXF, or .EPS

SH_Type_C_212 .DWG, .DXF, or .EPS

Each of these drawings are available on the Anvil web site in CAD format. The file name at the bottom of each box refers to that CAD file.

32

Anvil International, Piping & Pipe Hanger Design and Engineering

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E NGINEERED H ANGER A PPLICATIONS

Spring Hanger Assemblies (continued)

55L

55L

82, 268, 98 TYPE D

82, 268, 98 TYPE D

140, 146

140, 146

291 82, 268, 98 TYPE C

82, 268, 98 TYPE C

140, 146

140, 146 299

290

299 290

53-SD WELD LUG

53-SD WELD LUG

295, 295A, 295H

295, 295A, 295H

ELBOW SH_Type_C_295 .DWG, .DXF, or .EPS

ELBOW

SH_Type_C_53SD .DWG, .DXF, or .EPS

SH_Type_D_295 .DWG, .DXF, or .EPS

SH_Type_D_53SD .DWG, .DXF, or .EPS

82, 268, 98 TYPE E

PIPE STANCHION 63 PIPE SLIDE 140, 146

82, 268, 98 TYPE F

82, 268, 98 TYPE F, WITH PIPE ROLLER

82, 268, 98 TYPE F

290 295, 295A, 295H

SH_Type_E .DWG, .DXF, or .EPS

SH_Type_F_PipeSlide .DWG, .DXF, or .EPS

SH_Type_F_PipeRoller .DWG, .DXF, or .EPS

SH_Type_F_63 .DWG, .DXF, or .EPS

ELBOW

66

66 290

290 PIPE STANCHION 62

C-C (NEEDED)

C-C (NEEDED)

140, 146 137 S

140, 146

160-166A

82, 268, 98 TYPE F

82, 268, 98 TYPE G

82, 268, 98 TYPE G

60 SH_Type_F_62 .DWG, .DXF, or .EPS

SH_Type_G .DWG, .DXF, or .EPS

SH_Type_G_160-137S.DWG, .DXF, or .EPS

Each of these drawings are available on the Anvil web site in CAD format. The file name at the bottom of each box refers to that CAD file.

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Anvil International, Piping & Pipe Hanger Design and Engineering

33

R IGID H ANGER A PPLICATIONS

Rigid Hanger Assemblies

66 290

66 290 C-C (NEEDED)

66 290 FIG. 230 TURNBUCKLE AND FIG. 253 ROD MAY BE ADDED FOR VERTICAL ADJUSTMENT

66 290 253

253

230 230

140, 146

140, 146

140, 146

290

140

299

290

53-SD WELD LUG

295, 295A, 295H

212, 216 290

ELBOW

40 RH_212_290_140_66.DWG, .DXF, or .EPS

RH_40_290_230_Riser.DWG, .DXF, or .EPS

RH_295_290_230.DWG, .DXF, or .EPS

RH_53SD_299_290.DWG, .DXF, or .EPS

60

55 LUG 299

66

140, 146

140, 146

290

290

55 LUG 299

140, 146

140, 146 290 295, 295A, 295H

212, 216

212, 216 260

RH_212_290.DWG, .DXF, or .EPS

RH_260_140_60.DWG, .DXF, or .EPS

RH_212_290_299_55.DWG, .DXF, or .EPS

RH_295_290_299_55.DWG, .DXF, or .EPS 60

66 290 C-C (NEEDED)

C-C (NEEDED)

140, 146 45 BACK/BACK CHANNEL SIZED BY CUSTOMERS TO MEET LOAD REQ. 230 137S 140, 146

137S

ALTERNATE ORIENTATION OF 137S/PIPE

140, 146

60 RH_45_137S_66_Trapeze .DWG, .DXF, or .EPS

45 BACK/BACK CHANNEL SIZED BY CUSTOMERS TO MEET LOAD REQ. ALTERNATE ORIENTATION OF 137S/PIPE

60 RH_45_137S_60_Trapeze .DWG, .DXF, or .EPS

Each of these drawings are available on the Anvil web site in CAD format. The file name at the bottom of each box refers to that CAD file.

34

Anvil International, Piping & Pipe Hanger Design and Engineering

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R IGID H ANGER A PPLICATIONS

Rigid Hanger Assemblies (continued)

218

218

218

157

157

157

140, 146

140, 146

140, 146

92, 93

140, 146

181 65, CT-65, 260

65, 260

65, CT-65, 260 167

167

RH_181_157_218.DWG, .DXF, or .EPS

RH_167_65_157_218.DWG, .DXF, or .EPS

RH_65_157_218.DWG, .DXF, or .EPS

228, 292

228, 292

RH_167_65_92.DWG, .DXF, or .EPS

218

228, 292

157 HOT SERVICE UP TO 4" INSULATION

140, 146 140, 146

140, 146 290

290 140, 146

295, 295A, 295H

212, 216

260

RH_295_290_228.DWG, .DXF, or .EPS

69, CT-69, 70

RH_212_290_228.DWG, .DXF, or .EPS

RH_260_228.DWG, .DXF, or .EPS

RH_69_157_218.DWG, .DXF, or .EPS

60

86

66 290

92, 93, 94 HOT SERVICE UP TO 4" INSULATION 140, 146

140, 146

65, CT-65, 260

RH_65_86.DWG, .DXF, or .EPS

140, 146

140, 146

290

290

295, 295A, 295H

295, 295A, 295H

69, CT-69, 70

RH_69_92.DWG, .DXF, or .EPS

RH_295_290_60.DWG, .DXF, or .EPS

RH_295_290_66.DWG, .DXF, or .EPS

Each of these drawings are available on the Anvil web site in CAD format. The file name at the bottom of each box refers to that CAD file.

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Anvil International, Piping & Pipe Hanger Design and Engineering

35

R IGID H ANGER A PPLICATIONS

Rigid Hanger Assemblies (continued) 60

66 290 140, 146

FIG. 230 TURNBUCKLE AND FIG. 253 ROD MAY BE ADDED FOR VERTICAL ADJUSTMENT

MEDIUM SERVICE MAX. SERVICE TEMP. 650 FOR PIPE CLAMP 140, 146

140, 146 65, 260

290 212, 216

260

167 RH_167_65_60.DWG, .DXF, or .EPS

RH_260_290_66.DWG, .DXF, or .EPS

281, 282, 285

RH_212_290_60.DWG, .DXF, or .EPS

281, 282, 285

281, 282, 285

140, 146

140, 146 140, 146

65, 260

65, CT-65, 260

69, CT-69, 70

167, SEE SELECTION CHART RH_69_281_CI .DWG, .DXF, or .EPS

RH_167_65_281_CI .DWG, .DXF, or .EPS

RH_65_281_CI .DWG, .DXF, or .EPS

140, 146

140, 146

140, 146

181 65, CT-65, 260

69, CT-69, 70

167

RH_69_60.DWG, .DXF, or .EPS

RH_160_181_60.DWG, .DXF, or .EPS

160 (1" INSUL.) 161 (11⁄2" INSUL.) 162 (2" INSUL.) 163 (21⁄2" INSUL.) 164 (3" INSUL.) 165 (4" INSUL.) RH_167_260_60.DWG, .DXF, or .EPS

Each of these drawings are available on the Anvil web site in CAD format. The file name at the bottom of each box refers to that CAD file.

36

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W EIGHT W EIGHTS

OF

OF

P IPING M ATERIALS

P IPING M ATERIALS – I NTRODUCTION

The tabulation of weights of standard piping materials presented on the following pages has been arranged for convenience of selection of data that formerly consumed considerable time to develop. For special materials, the three formulae listed below for weights of tubes, weights of contents of tubes, and weights of piping insulation will be helpful. Weight of tube = F x 10.68 x T x (D - T) Ib/ft

T = wall thickness in inches D = outside diameter in inches F = relative weight factor The weight of tube furnished in this piping data is based on low carbon steel weighing 0.2833 lb/in3.

The weight of welding tees and laterals are for full size fittings. The weights of reducing fittings are approximately the same as for full size fittings. The weights of welding reducers are for one size reduction, and are approximately correct for other reductions. Weights of valves of the same type may vary because of individual manufacturer's designs. Listed valve weights are approximate only. Specific valve weights should be used when available. Where specific insulation thicknesses and densities differ from those shown, refer to "Weight of Piping Insulation" formula below.

W EIGHT

OF PIPING INSULATION

Pipe Insulation Weight = I x .0218 x T x (D+T ) Ib/ft

R ELATIVE W EIGHT F ACTOR F Aluminum ............................... 0.35

I = insulation density in pounds per cubic foot

Brass ..................................... 1.12

T = insulation thickness in inches

Cast Iron ................................ 0.91

D = outside diameter of pipe in inches

Copper ................................... 1.14 Ferritic stainless steel ........... 0.95 Austenitic stainless steel ....... 1.02 Steel ...................................... 1.00 Wrought iron .......................... 0.98

W EIGHT

OF CONTENTS OF A TUBE

Weight of Tube Contents = G x .3405 x (D - 2T)2 Ib/ft G = specific gravity of contents T = tube wall thickness in inches D = tube outside diameter in inches

3

⁄8 ⁄2 5 ⁄8 3 ⁄4 7 ⁄8 1 11⁄4 11⁄2 13⁄4 2 21⁄4 21⁄2 23⁄4 3 31⁄4 31⁄2 33⁄4 4 41⁄4 41⁄2 43⁄4 5 1

W EIGHT T OLERANCES The weight per foot of steel pipe is subject to the following tolerances: SPECIFICATION ................... TOLERANCE ASTM A-120 & ASTM A-53 STD WT ........................... +5% XS WT .............................. +5% XXS WT .......................... +10%

-5% -5% -10%

ASTM A-106 SCH 10-120 ................... +6.5% SCH 140-160 .................. +10%

-3.5% -3.5%

ASTM A-335 12" and under ................ +6.5% over l2" ............................ +10%

-3.5% -5%

ASTM A-312 & ASTM A-376 12"and under .................. +6.5%

-3.5%

API 5L All sizes .................... +6.5%

-3.5%

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TABLE III - LOAD CAPACITY OF THREADED HANGER RODS IN ACCORDANCE WITH MSS-SP58 Nominal Root Area Max Recommended Rod Diam. of Coarse Thread Load at Rod Temp 650° Inch Sq. In. Lbs 0.068 0.126 0.202 0.302 0.419 0.551 0.890 1.29 1.74 2.30 3.02 3.72 4.62 5.62 6.72 7.92 9.21 10.6 12.1 13.7 15.4 17.2

730 1,350 2,160 3,230 4,480 5,900 9,500 13,800 18,600 24,600 32,300 39,800 49,400 60,100 71,900 84,700 98,500 114,000 129,000 146,000 165,000 184,000

Anvil International, Piping & Pipe Hanger Design and Engineering

37

W EIGHT

OF

P IPING M ATERIALS – 1" P IPE (1.313" O.D.)

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt

5S 0.065 0.868

PIPE 10S 0.109 1.404

40/Std. 0.133 1.68

80/XS 0.179 2.17

160 0.25 2.84

XXS 0.358 3.66

Water -- Lbs/Ft

0.478

0.409

0.37

0.31

0.23

0.12

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

0.2 0.3

0.4 0.3

0.4 0.3

0.4 0.3

0.6 0.3

1.0 0.3

0.3 0.2

S.R. 90° Elbow L.R. 45° Elbow

0.1 0.2

0.3 0.2

0.3 0.2

0.3 0.2

0.4 0.2

0.5 0.2

Tee

0.4 0.4

0.6 0.4

0.8 0.4

0.9 0.4

1.1 0.4

1.3 0.4

Lateral

0.7 1.1

1.2 1.1

1.7 1.1

2.5 1.1

Reducer

0.2 0.2

0.4 0.2

0.3 0.2

0.4 0.2

0.5 0.2

0.5 0.2

Cap

0.1 0.3

0.1 0.3

0.3 0.3

0.3 0.3

0.4 0.3

0.5 0.3

200-299 1 0.72

300-399 11⁄2 1.23

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 1 0.72

PIPE INSULATION 400-499 500-599 2 2 1.94 1.94

600-699

700-799

800-899

21⁄2 3.3

21⁄2 3.3

21⁄2 3.3

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI)

Cast Iron 125 250

––––––––––––––––– Steel –––––––––––– 150 300 400 600 900 1500 2500

2.3 1.5

2.5 1.5

4

5

5

12

12

15

1.5

1.5

1.5

1.5

1.5

1.5

Welding Neck

3 1.5

5 1.5

7 1.5

7 1.5

12 1.5

12 1.5

16 1.5

Lap Joint

2.5 1.5

4 1.5

5 1.5

5 1.5

12 1.5

12 1.5

15 1.5

2.5 1.5

5 1.5

5 1.5

5 1.5

12 1.5

12 1.5

15 1.5

Screwed or Slip-On

Blind

2.5 1.5

4 1.5

5 1.5

15 3.7

28 3.8

45° Elbow

14 3.4

26 3.6

Tee

20 5.6

39 5.7

25 1.5

80 4.3

S.R. 90° Elbow L.R. 90° Elbow

Flanged Bonnet Gate

20 1.2

Flanged Bonnet – Globe or Angle

84 3.5

Flanged Bonnet – Check Pressure Seal – Bonnet, Gate

31 1.7

900-999 1,000-1,099 1,100-1,200

3 4.7

3 4.7

3 4.7

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

31 1.7

Pressure Seal – Bonnet, Globe

38

Anvil International, Piping & Pipe Hanger Design and Engineering

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W EIGHT

OF

P IPING M ATERIALS – 1 1 ⁄ 4" P IPE (1.660" O.D.)

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt Water -- Lbs/Ft

5S 0.065 1.11

PIPE 10S 0.109 1.81

40/Std. 0 2.27

80/XS 0.191 3.00

160 0 3.77

XXS 0.382 5.22

0.8

0.71

0.65

0.56

0.46

0.27

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

0.3 0.3

0.5 0.3

0.6 0.3

0.8 0.3

1 0.3

1.3 0.3

0.4 0.2

S.R. 90° Elbow L.R. 45° Elbow

0.2 0.2

0.3 0.2

0.3 0.2

0.5 0.2

0.6 0.2

0.7 0.2

Tee

0.7 0.5

1.1 0.5

1.6 0.5

1.6 0.5

1.9 0.5

2.4 0.5

Lateral

1.1 1.2

1.9 1.2

2.4 1.2

3.8 1.2

Reducer

0.3 0.2

0.4 0.2

0.5 0.2

0.6 0.2

0.7 0.2

0.8 0.2

Cap

0.1 0.3

0.1 0.3

0.4 0.3

0.4 0.3

0.6 0.3

0.6 0.3

200-299 1 0.65

300-399 11⁄2 1.47

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 1 0.65

PIPE INSULATION 400-499 500-599 2 2 1.83 1.83

600-699 21⁄2 2.65 21⁄2 3.17

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel ––––––––––––– 125 250 150 300 400 600 900 1500 2500 3.5 1.5

5 1.5

7 1.5

7 1.5

13 1.5

13 1.5

23 1.5

Welding Neck

3 1.5

7 1.5

8 1.5

8 1.5

13 1.5

13 1.5

25 1.5

Lap Joint

3.5 1.5

5 1.5

7 1.5

7 1.5

13 1.5

13 1.5

22 1.5

3.5 1.5

4 1.5

7 1.5

7 1.5

13 1.5

13 1.5

23 1.5

Screwed or Slip-On

Blind

2.5 1.5

2.8 1.5

4.8 1.5

5.5 1.5

S.R. 90° Elbow

17 3.7

18 3.8

33 3.9

L.R. 90° Elbow

18 3.9

45° Elbow

15 3.4

16 3.5

31 3.7

Tee

23 5.6

28 5.7

49 5.9

Flanged Bonnet Gate

40 4

60 4.2

97 4.6

Flanged Bonnet – Globe or Angle Flanged Bonnet – Check Pressure Seal – Bonnet, Gate

21 4 38 1.1

700-799 21⁄2 2.65 21⁄2 3.17

800-899 21⁄2 2.65 21⁄2 3.17

900-999 1,000-1,099 1,100-1,200 3 3 3 3.58 3.58 3.58 3 3 3 5.76 5.76 5.76

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

38 1.1

Pressure Seal – Bonnet, Globe

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Anvil International, Piping & Pipe Hanger Design and Engineering

39

W EIGHT

OF

P IPING M ATERIALS – 1 1 ⁄ 2" P IPE (1.900" O.D.)

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt

5S 0.065 1.27

10S 0.109 2.09

PIPE 40/Std. 0.145 2.72

80/XS 0.200 3.63

160 0.281 4.86

XXS 0.400 6.41

0.525 7.71

0.650 8.68

Water -- Lbs/Ft

1.07

0.96

0.88

0.77

0.61

0.41

0.25

0.12

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

0.4 0.4

0.8 0.4

S.R. 90° Elbow

0.9 0.4

1.2 0.4

0.6 0.3

0.8 0.3

1.5 0.4

2.0 0.4

L.R. 45° Elbow

0.3 0.2

0.5 0.2

0.5 0.2

0.7 0.2

0.8 0.2

1.0 0.2

Tee

0.9 0.6

1.5 0.6

2.0 0.6

2.4 0.6

3.0 0.6

3.7 0.6

Lateral

1.3 1.3

2.1 1.3

3.3 1.3

5.5 1.3

Reducer

0.3 0.2

0.6 0.2

0.6 0.2

0.8 0.2

1.0 0.2

1.2 0.2

Cap

0.1 0.3

0.2 0.3

0.4 0.3

0.5 0.3

0.7 0.3

0.8 0.3

200-299 1 0.84

300-399 11⁄2 1.35

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 1 0.84

PIPE INSULATION 400-499 500-599 2 2 2.52 2.52

600-699 21⁄2 3.47 21⁄2 4.2

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI)

Cast Iron 125 250

––––––––––––––––– Steel –––––––––––– 150 300 400 600 900 1500 2500

3 1.5

3.5 1.5

6 1.5

9 1.5

9 1.5

19 1.5

19 1.5

31 1.5

Welding Neck

4.5 1.5

8 1.5

12 1.5

12 1.5

19 1.5

19 1.5

34 1.5

Lap Joint

3.5 1.5

6 1.5

9 1.5

9 1.5

19 1.5

19 1.5

30 1.5

3.5 1.5

8 1.5

10 1.5

10 1.5

19 1.5

19 1.5

31 1.5

Screwed or Slip-On

6 1.5

Blind

4 1.5

6 1.5

S.R. 90° Elbow

9 3.7

12 3.7

23 3.8

L.R. 90° Elbow

12 4

13 4

24 4

45° Elbow

8 3.4

11 3.4

Tee

15 5.6

20 5.6

Flanged Bonnet Gate

27 6.8

Flanged Bonnet – Globe or Angle Flanged Bonnet – Check Pressure Seal – Bonnet, Gate

30 4.1

26 3.9

46 4

21 3.5

23 3.5

39 3.7

30 5.7

37 5.8

70 6

55 4.2

70 4.5

125 5

40 4.2

45 4.2

170 5

35 4.1

40 4.2

110 4.5 42 1.9

700-799 21⁄2 3.47 21⁄2 4.2

800-899 21⁄2 3.47 21⁄2 4.2

900-999 1,000-1,099 1,100-1,200 3 3 3 4.52 4.52 4.52 3 3 3 5.62 5.62 5.62

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

42 1.2

Pressure Seal – Bonnet, Globe

40

Anvil International, Piping & Pipe Hanger Design and Engineering

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W EIGHT

OF

P IPING M ATERIALS – 2" P IPE (2.375" O.D.)

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt

5S 0.065 1.60

10S 0.109 2.64

PIPE 40/Std. 0.154 3.65

80/XS 0.218 5.02

160 0.343 7.44

XXS 0.436 9.03

0.562 10.88

0.687 12.39

Water -- Lbs/Ft

1.72

1.58

1.46

1.28

0.97

0.77

0.53

0.34

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

0.6 0.5

1.1 0.5

S.R. 90° Elbow

1.5 0.5

2.1 0.5

1.0 0.3

1.4 0.3

3.0 0.5

4.0 0.5

L.R. 45° Elbow

0.4 0.2

0.6 0.2

0.9 0.2

1.1 0.2

1.6 0.2

2.0 0.2

Tee

1.1 0.6

1.8 0.6

2.9 0.6

3.7 0.6

4.9 0.6

5.7 0.6

Lateral

1.9 1.4

3.2 1.4

5.0 1.4

7.7 1.4

Reducer

0.4 0.3

0.9 0.3

0.9 0.3

1.2 0.3

1.6 0.3

1.9 0.3

Cap

0.2 0.4

0.3 0.4

0.6 0.4

0.7 0.4

1.1 0.4

1.2 0.4

200-299 1 1.01

300-399 11⁄2 1.71

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 1 1.01

PIPE INSULATION 400-499 500-599 2 2 2.53 2.53

600-699 21⁄2 3.48 21⁄2 4.28

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI)

Cast Iron 125 250

––––––––––––––––– Steel –––––––––––– 150 300 400 600 900 1500 2500

5 1.5

6 1.5

9 1.5

11 1.5

11 1.5

32 1.5

32 1.5

49 1.5

Welding Neck

7 1.5

11 1.5

14 1.5

14 1.5

32 1.5

32 1.5

53 1.5

Lap Joint

6 1.5

9 1.5

11 1.5

11 1.5

32 1.5

32 1.5

48 1.5

12 1.5

12 1.5

32 1.5

32 1.5

50 1.5

Screwed or Slip-On

7 1.5

Blind

5 1.5

8 1.5

5 1.5

10 1.5

S.R. 90° Elbow

14 3.8

20 3.8

19 3.8

29 3.8

L.R. 90° Elbow

16 4.1

27 4.1

22 4.1

31 4.1

45° Elbow

12 3.4

18 3.5

16 3.4

Tee

21 5.7

32 5.7

Flanged Bonnet Gate

37 6.9

Flanged Bonnet – Globe or Angle Flanged Bonnet – Check

35 4

83 4.2

24 3.5

33 3.7

73 3.9

27 5.7

41 5.7

52 6

129 6.3

52 7.1

40 4

65 4.2

80 4.5

190 5

30 7

64 7.3

30 3.8

45 4

85 4.5

235 5.5

26 7

51 7.3

35 3.8

40 4

60 4.2

300 5.8

Pressure Seal – Bonnet, Gate

150 2.5

Pressure Seal – Bonnet, Globe

165 3

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700-799 21⁄2 3.48 21⁄2 4.28

800-899 3 4.42 3 5.93

900-999 1,000-1,099 1,100-1,200 3 3 31⁄2 4.42 4.42 5.59 3 3 31⁄2 5.93 5.93 7.80

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

Anvil International, Piping & Pipe Hanger Design and Engineering

41

W EIGHT

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt Water -- Lbs/Ft

OF

P IPING M ATERIALS – 2 1⁄ 2" P IPE (2.875" O.D.)

5S 0.083 2.48

10S 0.120 3.53

PIPE 40/Std. 0.203 5.79

80/XS 0.276 7.66

160 0.375 10.01

XXS 0.552 13.70

0.675 15.86

0.800 17.73

2.5

2.36

2.08

1.84

1.54

1.07

0.79

0.55

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

1.2 0.6

1.8 0.6

S.R. 90° Elbow

3.0 0.6

3.8 0.6

2.2 0.4

2.5 0.4

5.0 0.6

7.0 0.6

L.R. 45° Elbow

0.7 0.3

1.0 0.3

1.6 0.3

2.1 0.3

3.0 0.3

3.5 0.3

Tee

2.1 0.8

3.0 0.8

5.2 0.8

6.4 0.8

7.8 0.8

9.8 0.8

Lateral

3.5 1.5

4.9 1.5

9.0 1.5

13 1.5

Reducer

0.6 0.3

1.2 0.3

1.6 0.3

2.0 0.3

2.7 0.3

3.3 0.3

Cap

0.3 0.4

0.4 0.4

0.9 4.0

1.0 0.4

1.9 0.4

2.0 0.4

200-299 1 1.14

300-399 11⁄2 2.29

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 1 1.14

PIPE INSULATION 400-499 500-599 2 2 3.23 3.23

600-699 21⁄2 4.28 21⁄2 5.2

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

125

250

150

300

400

600

900 1500 2500

7 1.5

12.5 1.5

8 1.5

14 1.5

17 1.5

17 1.5

46 1.5

46 1.5

69 1.5

Welding Neck

11 1.5

16 1.5

22 1.5

22 1.5

46 1.5

46 1.5

66 1.5

Lap Joint

8 1.5

14 1.5

16 1.5

16 1.5

45 1.5

45 1.5

67 1.5

19 1.5

19 1.5

45 1.5

45 1.5

70 1.5

Screwed or Slip-On

42

Blind

7.8 1.5

10 1.5

8 1.5

16 1.5

S.R. 90° Elbow

20 3.8

33 3.9

27 3.8

42 3.9

L.R. 90° Elbow

24 4.2

30 4.2

47 4.2

45° Elbow

18 3.5

31 3.6

22 3.5

Tee

31 5.7

49 5.8

Flanged Bonnet Gate

50 7

Flanged Bonnet – Globe or Angle Flanged Bonnet – Check

50 4.1

114 4.4

35 3.6

46 3.8

99 3.9

42 5.7

61 5.9

77 6.2

169 6.6

82 7.1

60 4

100 4.2

105 4.6

275 5.2

43 7.1

87 7.4

50 4

70 4.1

120 4.6

325 5.5

36 7.1

71 7.4

40 4

50 4

105 4.6

320 5.5

Pressure Seal – Bonnet, Gate

215 2.5

Pressure Seal – Bonnet, Globe

230 2.8

Anvil International, Piping & Pipe Hanger Design and Engineering

700-799 21⁄2 4.28 21⁄2 5.2

800-899 3 5.46 3 7.36

900-999 1,000-1,099 1,100-1,200 3 31⁄2 31⁄2 5.46 6.86 6.86 3 31⁄2 31⁄2 7.36 9.58 9.58

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

www.anvilintl.com

W EIGHT

OF

P IPING M ATERIALS – 3" P IPE (3.500" O.D.)

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt

5S 0.083 3.03

10S 0.120 4.33

PIPE 40/Std. 0.216 7.58

80/XS 0.300 10.25

160 0.438 14.32

XXS 0.600 18.58

0.725 21.49

0.850 24.06

Water -- Lbs/Ft

3.78

3.61

3.20

2.86

2.35

1.80

1.43

1.10

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

1.7 0.8

2.5 0.8

S.R. 90° Elbow

4.7 0.8

6.0 0.8

3.3 0.5

4.1 0.5

8.5 0.8

11.0 0.8

L.R. 45° Elbow

0.9 0.3

1.3 0.3

2.5 0.3

3.3 0.3

4.5 0.3

5.5 0.3

Tee

2.7 0.8

3.9 0.8

7.0 0.8

10.0 0.8

12.2 0.8

14.8 0.8

Lateral

4.5 1.8

6.4 1.8

12.5 1.8

18.0 1.8

Reducer

0.8 0.3

1.5 0.3

2.1 0.3

2.8 0.3

3.7 0.3

4.6 0.3

Cap

0.5 0.5

0.7 0.5

1.4 0.5

1.8 0.5

3.5 0.5

3.6 0.5

200-299 1 1.25

300-399 11⁄2 2.08

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 1 1.25

PIPE INSULATION 400-499 500-599 2 2 3.01 3.01

600-699 21⁄2 4.07 21⁄2 5.07

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

125

250

150

300

400

600

900 1500 2500

8.6 1.5

15.8 1.5

9 1.5

17 1.5

20 1.5

20 1.5

37 1.5

61 1.5

102 1.5

Welding Neck

12 1.5

19 1.5

27 1.5

27 1.5

38 1.5

61 1.5

113 1.5

Lap Joint

9 1.5

17 1.5

19 1.5

19 1.5

36 1.5

60 1.5

99 1.5

24 1.5

24 1.5

38 1.5

61 1.5

105 1.5

67 4.1

98 4.3

150 4.6

Screwed or Slip-On

Blind

9 1.5

17.5 1.5

10 1.5

20 1.5

S.R. 90° Elbow

25 3.9

44 4

32 3.9

53 4

L.R. 90° Elbow

29 4.3

40 4.3

63 4.3

45° Elbow

21 3.5

39 3.6

28 3.5

46 3.6

60 3.8

93 3.9

135 4

Tee

38 5.9

62 6

52 5.9

81 6

102 6.2

151 6.5

238 6.9

Flanged Bonnet Gate

66 7

112 7.4

70 4

125 4.4

155 4.8

260 5

410 5.5

Flanged Bonnet – Globe or Angle

56 7.2

87 7.6

60 4.3

95 4.5

155 4.8

225 5

495 5.5

Flanged Bonnet – Check

46 7.2

100 7.6

60 4.3

70 4.4

120 4.8

150 4.9

440 5.8

Pressure Seal – Bonnet, Gate

208 3

235 3.2

Pressure Seal – Bonnet, Globe

135 2.5

180 3

www.anvilintl.com

700-799 3 5.24 3 6.94

800-899 3 5.24 3 6.94

900-999 1,000-1,099 1,100-1,200 3 31⁄2 31⁄2 5.24 6.65 6.65 3 31⁄2 31⁄2 6.94 9.17 9.17

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

Anvil International, Piping & Pipe Hanger Design and Engineering

43

W EIGHT

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt

PIPE 5S 10S 0.083 0.120 3.47 4.97

Water -- Lbs/Ft

5.01

OF

P IPING M ATERIALS – 3 1⁄ 2" P IPE (4.000" O.D.)

40/Std. 0.226 9.11

80/XS 0.318 12.51

160 0.636 22.85

4.28

3.85

2.53

4.81

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

2.4 0.9

3.4 0.9

S.R. 90° Elbow

6.7 0.9

8.7 0.9

4.2 0.6

5.7 0.6

15.0 0.9

L.R. 45° Elbow

1.2 4.0

1.7 0.4

3.3 0.4

4.4 0.4

8.0 0.4

Tee

3.4 0.9

4.9

10.3 0.9

13.8 0.9

20.2 0.9

Lateral

6.2 1.8

8.9 1.8

17.2 1.8

25.0 1.8

Reducer

1.2 0.3

2.1 0.3

3.0 0.3

4.0 0.3

6.8 0.3

Cap

0.6 0.6

0.8 0.6

2.1 0.6

2.8 0.6

5.5 0.6

200-299 1 1.83

300-399 11⁄2 2.77

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 1 1.83

PIPE INSULATION 400-499 500-599 2 21⁄2 3.71 4.88

600-699 21⁄2 4.88 21⁄2 6.49

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

125

250

150

300

400

600

11 1.5

20 1.5

13 1.5

21 1.5

27 1.5

27 1.5

Welding Neck

14 1.5

22 1.5

32 1.5

32 1.5

Lap Joint

13 1.5

21 1.5

26 1.5

26 1.5

15 1.5

25 1.5

35 1.5

35 1.5

Screwed or Slip-On

Blind

13 1.5

S.R. 90° Elbow

33 4

23 1.5

49 4

82 4.3

54 4.4

L.R. 90° Elbow 45° Elbow

29 3.6

39 3.6

75 3.6

Tee

51 6

103 6.2

70 6

133 6.4

Flanged Bonnet Gate

82 7.1

143 7.5

90 4.1

Flanged Bonnet – Globe or Angle

74 7.3

137 7.7

160 4.7

Flanged Bonnet – Check

71 7.3

125 7.7

125 4.7

Pressure Seal – Bonnet, Gate

900 1500 2500

155 4.5

180 4.8

140 2.5

360 5

510 5.5

295 2.8

380 3

700-799 3 6.39 3 8.71

800-899 3 6.39 3 8.71

900-999 1,000-1,099 1,100-1,200 31⁄2 31⁄2 31⁄2 7.80 7.80 7.80 31⁄2 31⁄2 31⁄2 10.8 10.8 10.8

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

Pressure Seal – Bonnet, Globe

44

Anvil International, Piping & Pipe Hanger Design and Engineering

www.anvilintl.com

W EIGHT

OF

P IPING M ATERIALS – 4" P IPE (4.500" O.D.)

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt

5S 0.083 3.92

10S 0.12 5.61

0.188 8.56

Water -- Lbs/Ft

6.40

6.17

5.80

PIPE 40/STD. 80/XS 0.237 0.337 10.79 14.98 5.51

4.98

120 0.438 18.96

0.500 21.36

160 0.531 22.51

XXS 0.674 27.54

0.800 31.61

0.925 35.32

4.48

4.16

4.02

3.38

2.86

2.39

18.0 1.0

20.5 1.0

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

3.0 1.0

4.3 1.0

S.R. 90° Elbow

8.7 1.0

12.0 1.0

6.7 0.7

8.3 0.7

L.R. 45° Elbow

1.5 0.4

2.2 0.4

4.3 0.4

5.9 0.4

8.5 0.4

10.0 4.0

Tee

3.9 1.0

5.7 1.0

13.5 1.0

16.4 1.0

22.8 1.0

26.6 1.0

Lateral

6.6 2.1

10.0 2.1

20.5 2.1

32.0 2.1

Reducer

1.2 0.3

2.4 0.3

3.6 0.3

4.8 0.3

6.6 0.3

8.2 0.3

Cap

0.8 0.3

1.2 0.3

2.5 0.5

3.4 0.5

6.5 6.5

6.6 6.6

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 1 1.62

200-299 1 1.62

300-399 11⁄2 2.55

PIPE INSULATION 400-499 500-599 2 21⁄2 3.61 4.66

600-699 21⁄2 4.66 21⁄2 6.07

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI)

Cast Iron 125 250

––––––––––––––––– Steel –––––––––––– 150 300 400 600 900 1500 2500

14 1.5

15 1.5

26 1.5

32 1.5

43 1.5

66 1.5

90 1.5

158 1.5

Welding Neck

17 1.5

29 1.5

41 1.5

48 1.5

64 1.5

90 1.5

177 1.5

Lap Joint

15 1.5

26 1.5

31 1.5

42 1.5

64 1.5

92 1.5

153 1.5 164 1.5

Screwed or Slip-On

24 1.5

Blind

16 1.5

27 1.5

19 1.5

31 1.5

39 1.5

47 1.5

67 1.5

90 1.5

S.R. 90° Elbow

43 4.1

69 4.2

59 4.1

85 4.2

99 4.3

128 4.4

185 4.5

254 4.8

L.R. 90° Elbow

50 4.5

72 4.5

98 4.5

45° Elbow

38 3.7

62 3.8

51 3.7

78 3.8

82 3.9

119 4

170 4.1

214 4.2

Tee

66 6.1

103 6.3

86 6.1

121 6.3

153 6.4

187 6.6

262 6.8

386 7.2

Flanged Bonnet Gate

109 7.2

188 7.5

100 4.2

175 4.5

195 5

255 5.1

455 5.4

735 6

Flanged Bonnet – Globe or Angle

97 7.4

177 7.8

95 4.3

145 4.8

215 5

230 5.1

415 5.5

800 6

Flanged Bonnet – Check

80 7.4

146 7.8

80 4.3

105 4.5

160 4.8

195 5

320 5.6

780 6

215 2.8

380 3

520 4

240 2.7

290 3

Pressure Seal – Bonnet, Gate Pressure Seal – Bonnet, Globe

www.anvilintl.com

700-799 3 6.07 3 8.3

800-899 3 6.07 3 8.3

900-999 1,000-1,099 1,100-1,200 31⁄2 31⁄2 4 7.48 7.48 9.10 31⁄2 31⁄2 31⁄2 10.6 10.6 10.6

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

Anvil International, Piping & Pipe Hanger Design and Engineering

45

W EIGHT

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt

5S 0.109 6.35

10S 0.134 7.77

Water -- Lbs/Ft

9.73

9.53

PIPE 40/Std 80/XS 0.258 0.375 14.62 20.78 8.66

7.89

OF

P IPING M ATERIALS – 5" P IPE (5.563" O.D.)

120 0.500 27.04

160 0.625 32.96

XXS 0.750 38.55

0.875 43.81

1.000 47.73

7.09

6.33

5.62

4.95

4.23

700-799 3 6.9 3 9.3

800-899 31⁄2 8.41 31⁄2 11.8

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

6.0 1.3

7.4 1.3

16.0 1.3

21.4 1.3

S.R. 90° Elbow

4.2 0.8

5.2 0.8

10.4 0.8

14.5 0.8

L.R. 45° Elbow

3.1 0.5

3.8 0.5

8.3 0.5

Tee

9.8 1.2

12.0 1.2

Lateral

15.3 2.5

Reducer Cap

Temp. Range --> 85% Magnesia Calcium Silicate Combination

33.0 1.3

34.0 1.3

10.5 0.5

14.0 0.5

18.0 0.5

19.8 1.2

26.9 1.2

38.5 1.2

43.4 1.2

18.4 2.5

31.0 2.5

49.0 2.5

2.5 0.4

4.3 0.4

5.9 0.4

8.3 0.4

12.4 0.4

14.2 0.4

1.3 0.7

1.6 0.7

4.2 0.7

5.7 0.7

11.0 0.7

11.0 0.7

200-299 11⁄2 2.92

300-399 11⁄2 2.92

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 1 1.86

PIPE INSULATION 400-499 500-599 2 21⁄2 4.08 5.38

600-699 21⁄2 5.38 21⁄2 7.01

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

125

250

150

300

400

600

900 1500 2500

17 1.5

28 1.5

18 1.5

32 1.5

37 1.5

73 1.5

100 1.5

162 1.5

259 1.5

Welding Neck

22 1.5

36 1.5

49 1.5

78 1.5

103 1.5

162 1.5

293 1.5

Lap Joint

18 1.5

32 1.5

35 1.5

71 1.5

98 1.5

168 1.5

253 1.5 272 1.5

Screwed or Slip-On

Blind

21 1.5

35 1.5

23 1.5

39 1.5

50 1.5

78 1.5

104 1.5

172 1.5

S.R. 90° Elbow

55 4.3

91 4.3

80 4.3

113 4.3

123 4.5

205 4.7

268 4.8

435 5.2

L.R. 90° Elbow

65 4.7

91 4.7

128 4.7

45° Elbow

48 3.8

80 3.8

66 3.8

98 3.8

123 4

180 4.2

239 4.3

350 4.5

Tee

84 6.4

139 6.5

119 6.4

172 6.4

179 6.8

304 7

415 7.2

665 7.8

Flanged Bonnet Gate

138 7.3

264 7.9

150 4.3

265 4.9

310 5.3

455 5.5

615 6

1340 7

Flanged Bonnet – Globe or Angle

138 7.6

247 8

155 4.3

215 5

355 5.2

515 5.8

555 5.8

950 6

Flanged Bonnet – Check

118 7.6

210 8

110 4.3

165 5

185 5

350 5.8

560 6

1150 7

350 3.1

520 3.8

865 4.5

280

450

4

4.5

Pressure Seal – Bonnet, Gate Pressure Seal – Bonnet, Globe

46

Anvil International, Piping & Pipe Hanger Design and Engineering

900-999 1,000-1,099 1,100-1,200 31⁄2 4 4 8.41 10.4 10.4 31⁄2 4 4 11.8 14.9 14.9

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

www.anvilintl.com

W EIGHT

P IPING M ATERIALS – 6" P IPE (6.625" O.D.)

OF

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt

5S 0.109 5.37

10 0.134 9.29

Water -- Lbs/Ft

13.98

13.74

0.219 15.02

PIPE 40/Std. 0.280 18.97

80/XS 0.432 28.57

120 0.562 36.39

160 0.718 45.30

XXS 0.864 53.20

1.000 60.01

1.125 66.08

13.10

12.51

11.29

10.30

9.20

8.20

7.28

6.52

55.0 1.6

62.0 1.5

26.0 0.6

30.0 0.6

59.0 1.4

68.0 1.4

18.8 0.5

21.4 0.5

17.5 0.9

17.5 0.9

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

8.9 1.5

11.0 1.5

22.8 1.5

32.2 1.5

43.0 1.5

S.R. 90° Elbow

6.1 1.0

7.5 1.0

16.6 1.0

22.9 1.0

30.0 1.0

L.R. 45° Elbow

4.5 0.6

5.5 0.6

11.3 0.6

16.4 0.6

21.0 0.6

Tee

13.8 1.4

17.0 1.4

31.3 1.4

39.5 1.4

Lateral

16.7 2.9

20.5 2.9

42 2.9

78 2.9

Reducer

3.3 0.5

5.8 0.5

8.6 0.6

12.6 0.5

Cap

1.6 0.9

1.9 0.9

6.4 0.9

9.2 0.9

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 1 2.11

200-299 11⁄2 3.28

300-399 2 4.57

13.3 0.9

PIPE INSULATION 400-499 500-599 2 21⁄2 4.57 6.09

600-699 3 7.60 3 10.3

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

125

250

150

300

400

600

900 1500 2500

20 1.5

38 1.5

22 1.5

45 1.5

54 1.5

95 1.5

128 1.5

202 1.5

396 1.5

Welding Neck

27 1.5

48 1.5

67 1.5

96 1.5

130 1.5

202 1.5

451 1.5

Lap Joint

22 1.5

45 1.5

52 1.5

93 1.5

125 1.5

208 1.5

387 1.5 418 1.5

Screwed or Slip-On

Blind

26 1.5

48 1.5

29 1.5

56 1.5

71 1.5

101 1.5

133 1.5

197 1.5

S.R. 90° Elbow

71 4.3

121 4.4

90 4.3

147 4.4

184 4.6

275 4.8

375 5

566 5.3

L.R. 90° Elbow

88 4.9

126 4.9

182 4.9

45° Elbow

63 3.8

111 3.9

82 3.8

132 3.9

149 4.1

240 4.3

320 4.3

476 4.6

Tee

108 6.5

186 6.6

149 6.5

218 6.6

279 6.9

400 7.2

565 7.5

839 8

Flanged Bonnet Gate

172 7.3

359 8

190 4.3

360 5

435 5.5

620 5.8

835 6

1595 7

Flanged Bonnet – Globe or Angle

184 7.8

345 8.2

185 4.4

275 5

415 5.3

645 5.8

765 6

1800 7

Flanged Bonnet – Check

154 7.8

286 8.2

150 4.8

200 5

360 5.4

445 6

800 6.4

1630 7

580 3.5

750 4

1215 5

730 4

780 5

Pressure Seal – Bonnet, Gate Pressure Seal – Bonnet, Globe

www.anvilintl.com

700-799 3 7.60 3 10.3

800-899 31⁄2 9.82 31⁄2 13.4

900-999 1,000-1,099 1,100-1,200 31⁄2 4 4 9.82 11.5 11.4 31⁄2 4 4 13.4 16.6 16.6

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

Anvil International, Piping & Pipe Hanger Design and Engineering

47

W EIGHT

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt

5S 0.109 9.91

10S 0.148 13.40

Water -- Lbs/Ft

24.07

23.59

OF

P IPING M ATERIALS – 8" P IPE (8.625" O.D.)

0.219 19.64

20 0.250 22.36

PIPE 30 0.277 24.70

40/STD 0.322 28.55

60 0.406 35.64

80/XS 0.500 43.4

100 0.593 50.9

120 0.718 60.6

140 0.812 67.8

160 0.906 74.7

22.9

22.48

22.18

21.69

20.79

19.8

18.8

17.6

16.7

15.8

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

15.4 2.0

21 2.0

44.9 2.0

70.3 2.0

S.R. 90° Elbow

6.6 1.3

14.3 1.3

34.5 1.3

50.2 1.3

L.R. 45° Elbow

8.1 0.8

11.0 0.8

22.8 0.8

32.8 0.8

56.0 0.8

Tee

18.4 1.8

25.0 1.8

60.2 1.8

78.0 1.8

120.0 1.8

Lateral

25.3 3.8

41.1 3.8

76.0 3.8

140.0 3.8

Reducer

4.5 0.5

7.8 0.5

13.9 0.5

20.4 0.5

32.1 0.5

Cap

2.1 1.0

2.8 1.0

11.3 1.0

16.3 1.0

32.0 1.0

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 11⁄2 4.13

200-299 11⁄2 4.13

300-399 2 5.64

PIPE INSULATION 400-499 500-599 2 21⁄2 5.64 7.85

600-699 3 9.48 3 12.9

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

125

250

150

300

400

600

900 1500 2500

29 1.5

60 1.5

33 1.5

67 1.5

82 1.5

135 1.5

207 1.5

319 1.5

601 1.5

Welding Neck

42 1.5

76 1.5

104 1.5

137 1.5

222 1.5

334 1.5

692 1.5

Lap Joint

33 1.5

67 1.5

79 1.5

132 1.5

223 1.5

347 1.5

587 1.5 649 1.5

Screwed or Slip-On

Blind

43 1.5

79 1.5

48 1.5

90 1.5

115 1.5

159 1.5

232 1.5

363 1.5

S.R. 90° Elbow

113 4.5

194 4.7

157 4.5

238 4.7

310 5

435 5.2

639 5.4

995 5.7

L.R. 90° Elbow

148 5.3

202 5.3

283 5.3

45° Elbow

97 3.9

164 4

127 3.9

203 4

215 4.1

360 4.4

507 4.5

870 4.8

Tee

168 6.8

289 7.1

230 6.8

337 7.1

445 7.5

610 7.8

978 8.1

1465 8.6

Flanged Bonnet Gate

251 7.5

583 8.1

305 4.5

505 5.1

730 6

960 6.3

1180 2740 6.6 7

Flanged Bonnet – Globe or Angle

317 8.4

554 8.6

475 5.4

505 5.5

610 5.9

1130 1160 2865 6.3 6.3 7

Flanged Bonnet – Check

302 8.4

454 8.6

235 5.2

310 5.3

475 5.6

725 6

1140 2075 6.4 7

925 4.5

1185 2345 4.7 5.5

Pressure Seal – Bonnet, Gate Pressure Seal – Bonnet, Globe

48

700-799 31⁄2 11.5 31⁄2 16.2

120.0 2.0

800-899 31⁄2 11.5 31⁄2 16.2

900-999 1,000-1,099 1,100-1,200 4 4 41⁄2 13.8 13.8 16 4 4 41⁄2 20.4 20.4 23.8

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

1550 1680 4 5

Anvil International, Piping & Pipe Hanger Design and Engineering

www.anvilintl.com

W EIGHT

OF

P IPING M ATERIALS – 10" P IPE (10.750" O.D.)

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt

5S 0.134 15.15

10S 0.165 18.70

Water -- Lbs/Ft

37.4

36.9

0.219 24.63

20 0.250 28.04

PIPE 30 0.307 34.24

40/STD 0.365 40.5

60/XS 0.500 54.7

80 0.593 64.3

100 0.718 76.9

120 0.843 89.2

140 1.000 104.1

160 1.125 115.7

36.2

35.77

34.98

34.1

32.3

31.1

29.5

28.0

26.1

24.6

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

29.2 2.5

36.0 2.5

84.0 2.5

112.0 2.5

S.R. 90° Elbow

20.3 1.7

24.9 1.7

62.2 1.7

74.0 1.7

L.R. 45° Elbow

14.6 1.0

18.0 1.0

42.4 1.0

53.8 1.0

109.0 1.0

Tee

30.0 2.1

37.0 2.1

104.0 2.1

132.0 2.1

222.0 2.1

Lateral

47.5 4.4

70.0 4.4

124.0 4.4

200.0 4.4

Reducer

8.1 0.6

14.0 0.6

23.2 0.6

31.4 0.6

58.0 0.6

Cap

3.8 1.3

4.7 1.3

20.0 1.3

26.3 1.3

59.0 1.3

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 11⁄2 5.2

200-299 11⁄2 5.2

300-399 2 7.07

PIPE INSULATION 400-499 500-599 21⁄2 21⁄2 8.93 8.93

600-699 3 11 3 15.4

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

125

250

150

300

400

600

900 1500 2500

45 1.5

93 1.5

50 1.5

100 1.5

117 1.5

213 1.5

293 1.5

528 1.5

1148 1.5

Welding Neck

59 1.5

110 1.5

152 1.5

225 1.5

316 1.5

546 1.5

1291 1.5

Lap Joint

50 1.5

110 1.5

138 1.5

231 1.5

325 1.5

577 1.5

1120 1.5

599 1.5

1248 1.5

Screwed or Slip-On

Blind

66 1.5

120 1.5

77 1.5

146 1.5

181 1.5

267 1.5

338 1.5

S.R. 90° Elbow

182 4.8

306 4.9

240 4.8

343 4.9

462 5.2

747 5.6

995 5.8

L.R. 90° Elbow

237 5.8

290 5.8

438 5.8

45° Elbow

152 4.1

256 4.2

185 4.1

288 4.2

332 4.3

572 4.6

732 4.7

Tee

277 7.2

446 7.4

353 7.2

527 7.4

578 7.8

1007 1417 8.4 8.7

Flanged Bonnet Gate

471 7.7

899 8.3

455 4.5

750 5

1035 1575 2140 3690 6 6.9 7.1 8

Flanged Bonnet – Globe or Angle

541 9.1

943 9.1

485 4.5

855 5.5

1070 1500 2500 4160 6 6.3 6.8 8

Flanged Bonnet – Check

453 9.1

751 9.1

370 6

485 6.1

605 6.3

Pressure Seal – Bonnet, Gate Pressure Seal – Bonnet, Globe

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1030 1350 2280 6.8 7 7.5

230.0 2.5

700-799 31⁄2 13.2 31⁄2 19.3

800-899 31⁄2 13.2 31⁄2 19.3

900-999 1,000-1,099 1,100-1,200 4 4 41⁄2 15.5 15.5 18.1 4 4 41⁄2 23 23 27.2

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

1450 1860 3150 4.9 5.5 6 1800 1910 5 6

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P IPING M ATERIALS – 12" P IPE (12.750" O.D.)

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt

5S 0.156 20.99

10S 0.180 24.20

20 0.250 33.38

30 0.330 43.8

PIPE Std. 0.375 49.6

40 0.406 53.5

XS 0.500 65.4

60 0.562 73.2

80 0.687 88.5

120 1.000 125.5

140 1.125 139.7

160 1.312 160.3

Water -- Lbs/Ft

52.7

52.2

51.1

49.7

49.0

48.5

47.0

46.0

44.0

39.3

37.5

34.9

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

51.2 3.0

57.0 3.0

122.0 3.0

156.0 3.0

S.R. 90° Elbow

33.6 2.0

38.1 2.0

82.0 2.0

104.0 2.0

L.R. 45° Elbow

25.5 1.3

29.0 1.3

60.3 1.3

78.0 1.3

182.0 1.3

Tee

46.7 2.5

54.0 2.5

162.0 2.5

180.0 2.5

360.0 2.5

Lateral

74.7 5.4

86.2 5.4

180.0 5.4

273.0 5.4

Reducer

14.1 0.7

20.9 0.7

33.4 0.7

43.6 0.7

94.0 0.7

Cap

6.2 1.5

7.1 1.5

29.5 1.5

38.1 1.5

95.0 1.5

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 11⁄2 6.04

200-299 11⁄2 6.04

300-399 2 8.13

PIPE INSULATION 400-499 500-599 21⁄2 3 10.5 12.7

600-699 3 12.7 3 17.7

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

125

250

150

300

400

600

900 1500 2500

58 1.5

123 1.5

71 1.5

140 1.5

164 1.5

261 1.5

388 1.5

820 1.5

1611 1.5

Welding Neck

87 1.5

163 1.5

212 1.5

272 1.5

434 1.5

843 1.5

1919 1.5

Lap Joint

71 1.5

164 1.5

187 1.5

286 1.5

433 1.5

902 1.5

1573 1.5

928 1.5

1775 1.5

Screwed or Slip-On

Blind

95 1.5

165 1.5

117 1.5

209 1.5

261 1.5

341 1.5

475 1.5

S.R. 90° Elbow

257 5

430 5.2

345 5

509 5.2

669 5.5

815 5.8

1474 6.2

L.R. 90° Elbow

357 6.2

485 6.2

624 6.2

45° Elbow

227 4.3

360 4.3

282 4.3

414 4.3

469 4.5

705 4.7

Tee

387 7.5

640 7.8

513 7.5

754 7.8

943 8.3

1361 1928 8.7 9.3

Flanged Bonnet Gate

687 7.8

1298 8.5

635 4

1015 1420 2155 2770 4650 5 5.5 7 7.2 8

Flanged Bonnet – Globe or Angle

808 9.4

1200 9.5

710 5

1410 5.5

Flanged Bonnet – Check

674 9.4

1160 9.5

560 6

720 6.5

Pressure Seal – Bonnet, Gate

1598 6.2 1124 4.8

1410 2600 3370 7.2 8 8

375.0 3.0

700-799 31⁄2 15.1 31⁄2 21.9

800-899 4 17.9 4 26.7

900-999 1,000-1,099 1,100-1,200 4 41⁄2 41⁄2 17.9 20.4 20.4 4 41⁄2 41⁄2 26.7 31.1 31.1

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

1975 2560 4515 5.5 6 7

Pressure Seal – Bonnet, Globe

50

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P IPING M ATERIALS – 14" P IPE (14" O.D.)

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt

5S 0.156 23.0

10S 0.188 27.7

10 0.250 36.71

20 0.312 45.7

PIPE 30/Std. 0.375 54.6

40 0.438 63.4

XS 0.500 72.1

60 0.593 84.9

80 0.750 106.1

120 1.093 150.7

140 1.250 170.2

160 1.406 189.1

Water -- Lbs/Ft

63.7

63.1

62.06

60.92

59.7

58.7

57.5

55.9

53.2

47.5

45.0

42.6

700-799 31⁄2 15.8 31⁄2 22.8

800-899 4 18.5 4 27.5

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

65.6 3.5

78.0 3.5

157.0 3.5

200.0 3.5

S.R. 90° Elbow

43.1 2.3

51.7 2.3

108.0 2.3

135.0 2.3

L.R. 45° Elbow

32.5 1.5

39.4 1.5

80.0 1.5

98.0 1.5

Tee

49.4 2.8

59.6 2.8

196.0 2.8

220.0 2.8

Lateral

94.4 5.8

113 5.8

218.0 5.8

340.0 5.8

Reducer

25.0 1.1

31.2 1.1

63.0 1.1

83.0 1.1

Cap

7.6 1.7

9.2 1.7

35.3 1.7

45.9 1.7

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 11⁄2 6.16

200-299 11⁄2 6.16

300-399 2 8.38

PIPE INSULATION 400-499 500-599 21⁄2 3 10.7 13.1

600-699 3 13.1 3 18.2

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

125

250

150

300

400

600

900 1500 2500

90 1.5

184 1.5

95 1.5

195 1.5

235 1.5

318 1.5

460 1.5

1016 1.5

Welding Neck

130 1.5

217 1.5

277 1.5

406 1.5

642 1.5

1241 1.5

Lap Joint

119 1.5

220 1.5

254 1.5

349 1.5

477 1.5

1076 1.5

Screwed or Slip-On

Blind

125 1.5

239 1.5

141 1.5

267 1.5

354 1.5

437 1.5

574 1.5

S.R. 90° Elbow

360 5.3

617 5.5

497 5.3

632 5.5

664 5.7

918 5.9

1549 6.4

L.R. 90° Elbow

480 6.6

767 6.6

622 6.6

772 6.6

45° Elbow

280 4.3

497 4.4

377 4.3

587 4.4

638 4.6

883 4.8

1246 4.9

Tee

540 8

956 8.4

683 8

968 8.3

1131 1652 2318 8.6 8.9 9.6

Flanged Bonnet Gate

921 7.9

1762 8.8

905 4.9

1525 1920 2960 4170 6425 6 6.3 7 8 8.8

Flanged Bonnet – Globe or Angle

1171 9.9

Flanged Bonnet – Check

885 9.9

1010 5

1155 5.2

Pressure Seal – Bonnet, Gate

900-999 1,000-1,099 1,100-1,200 4 41⁄2 41⁄2 18.5 21.3 21.3 4 41⁄2 41⁄2 27.5 32.4 32.4

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

2620 3475 6380 6 6.5 7.5

Pressure Seal – Bonnet, Globe

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P IPING M ATERIALS – 16" P IPE (16" O.D.)

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt

5S 0.165 28.0

10S 0.188 32.0

10 0.250 42.1

20 0.312 52.4

PIPE 30/Std 0.375 62.6

40/XS 0.500 82.8

60 0.656 107.5

80 0.843 136.5

100 1.031 164.8

120 1.218 192.3

140 1.438 223.6

160 1.593 245.1

Water -- Lbs/Ft

83.5

83.0

81.8

80.5

79.1

76.5

73.4

69.7

66.1

62.6

58.6

55.9

700-799 31⁄2 17.5 31⁄2 25.2

800-899 4 20.5 4 30.7

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

89.8 4.0

102.0 4.0

208.0 4.0

270.0 4.0

S.R. 90° Elbow

59.7 2.5

67.7 2.5

135.0 2.5

177.0 2.5

L.R. 45° Elbow

44.9 1.7

51.0 1.7

104.0 1.7

136.0 1.7

Tee

66.8 3.2

75.9 3.2

250.0 3.2

278.0 3.2

Lateral

127.0 6.7

144.0 6.7

275.0 6.7

431.0 6.7

Reducer

31.3 1.2

35.7 1.2

77.0 1.2

102.0 1.2

Cap

10.1 1.8

11.5 1.8

44.3 1.8

57.0 1.8

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 11⁄2 6.90

200-299 11⁄2 6.90

300-399 2 9.33

PIPE INSULATION 400-499 500-599 21⁄2 3 12.0 14.6

600-699 3 14.6 3 20.3

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

125

250

150

300

400

600

900 1500 2500

114 1.5

233 1.5

107 1.5

262 1.5

310 1.5

442 1.5

559 1.5

1297 1.5

Welding Neck

141 1.5

288 1.5

351 1.5

577 1.5

785 1.5

1597 1.5

Lap Joint

142 1.5

282 1.5

337 1.5

476 1.5

588 1.5

1372 1.5

603 1.5

719 1.5

Screwed or Slip-On

Blind

174 1.5

308 1.5

184 1.5

349 1.5

455 1.5

S.R. 90° Elbow

484 5.5

826 5.8

656 5.5

958 5.8

1014 1402 1886 6 6.3 6.7

L.R. 90° Elbow

684 7

1036 7

781 7

1058 7

45° Elbow

374 4.3

696 4.6

481 4.3

708 4.6

Tee

714 8.3

1263 8.7

961 8.3

1404 1671 2128 3054 8.6 9 9.4 10

Flanged Bonnet Gate

1254 2321 1190 8 9 5

2015 2300 3675 4950 7875 7 7.2 7.9 8.2 9

1166 10.5

1225 6

839 4.7

1212 1586 5 5

Flanged Bonnet – Globe or Angle Flanged Bonnet – Check Pressure Seal – Bonnet, Gate

3230 7

900-999 1,000-1,099 1,100-1,200 4 41⁄2 41⁄2 20.5 23.6 23.6 4 41⁄2 41⁄2 30.7 36.0 36.0

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

8130 8

Pressure Seal – Bonnet, Globe

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P IPING M ATERIALS – 18" P IPE (18" O.D.)

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt

5S 0.165 31.0

10S 0.188 36.0

10 0.250 47.4

20 0.312 59.0

PIPE Std. 0.375 70.6

30 0.438 82.1

XS 0.500 93.5

40 0.562 104.8

60 0.750 138.2

80 0.937 170.8

120 1.375 244.1

160 1.781 308.5

Water -- Lbs/Ft

106.2

105.7

104.3

102.8

101.2

99.9

98.4

97.0

92.7

88.5

79.2

71.0

700-799 31⁄2 19.3 31⁄2 28

800-899 4 22.6 4 33.8

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION FACTOR L.R. 90° Elbow

114.0 4.5

129.0 4.5

256.0 4.5

332.0 4.5

S.R. 90° Elbow

75.7 2.8

85.7 2.8

176.0 2.8

225.0 2.8

L.R. 45° Elbow

57.2 1.9

64.5 1.9

132.0 1.9

168.0 1.9

Tee

83.2 3.6

94.7 3.6

282.0 3.6

351.0 3.6

Lateral

157.0 7.5

179.0 7.5

326.0 7.5

525.0 7.5

Reducer

42.6 1.3

48.5 1.3

94.0 1.3

123.0 1.3

Cap

12.7 2.1

14.5 2.1

57.0 2.1

75.0 2.1

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 11⁄2 7.73

200-299 11⁄2 7.73

300-399 2 10.4

PIPE INSULATION 400-499 500-599 21⁄2 3 13.3 16.3

600-699 3 16.3 3 22.7

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

125

150

300

400

600

900 1500 2500

139 1.5

331 1.5

380 1.5

573 1.5

797 1.5

Welding Neck

159 1.5

355 1.5

430 1.5

652 1.5

1074 2069 1.5 1.5

Lap Joint

165 1.5

355 1.5

415 1.5

566 1.5

820 1.5

572 1.5

762 1.5

1030 1.5

Screwed or Slip-On

250

125 1.5

Blind

209 1.5

396 1.5

228 1.5

440 1.5

S.R. 90° Elbow

599 5.8

1060 6

711 5.8

1126 1340 1793 2817 6 6.2 6.6 7

1350 7.4

941 7.4

1426 7.4

521 4.4

901 4.7

L.R. 90° Elbow 45° Elbow

439 4.4

870 4.7

Tee

879 8.6

1625 1010 9 8.6

1602 1909 2690 4327 9 9.3 9.9 10.5

Flanged Bonnet Gate

1629 2578 1510 8.2 9.3 6

2505 3765 4460 6675 6.5 7 7.8 8.5

1694 1.5

1769 1.5

1040 1543 2252 4.8 5 5.2

Flanged Bonnet – Globe or Angle Flanged Bonnet – Check Pressure Seal – Bonnet, Gate

1371 10.5

900-999 1,000-1,099 1,100-1,200 4 41⁄2 41⁄2 22.6 25.9 25.9 4 41⁄2 41⁄2 33.8 39.5 39.5

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

3100 3400 4200 5.5 5.6 6

Pressure Seal – Bonnet, Globe

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P IPING M ATERIALS – 20" P IPE (20" O.D.)

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt

5S 0.188 40.0

10S 0.218 46.0

10 0.250 52.7

20/Std. 0.375 78.6

PIPE 30/XS 0.500 104.1

40 0.593 122.9

60 0.812 166.4

80 1.031 208.9

100 1.281 256.1

120 1.500 296.4

140 1.750 341.1

160 1.968 379.0

Water -- Lbs/Ft

131.0

130.2

129.5

126.0

122.8

120.4

115.0

109.4

103.4

98.3

92.6

87.9

600-699 3 17.7 3 24.7

700-799 31⁄2 21.1 31⁄2 30.7

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

160.0 5.0

185.0 5.0

322.0 5.0

438.0 5.0

S.R. 90° Elbow

106.0 3.4

122.0 3.4

238.0 3.4

278.0 3.4

L.R. 45° Elbow

80.3 2.1

92.5 2.1

160.0 2.1

228.0 2.1

Tee

112.0 4.0

130.0 4.0

378.0 4.0

490.0 4.0

Lateral

228.0 8.3

265.0 8.3

396.0 8.3

625.0 8.3

Reducer

71.6 1.7

87.6 1.7

142.0 1.7

186.0 1.7

Cap

17.7 2.3

20.5 2.3

71.0 2.3

93.0 2.3

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 11⁄2 8.45

200-299 11⁄2 8.45

300-399 2 11.6

PIPE INSULATION 400-499 500-599 21⁄2 3 14.6 17.7

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

125

150

300

400

600

900 1500 2500

180 1.5

378 1.5

468 1.5

733 1.5

972 1.5

Welding Neck

195 1.5

431 1.5

535 1.5

811 1.5

1344 2614 1.5 1.5

Lap Joint

210 1.5

428 1.5

510 1.5

725 1.5

1048 2189 1.5 1.5

711 1.5

976 1.5

1287 1.5

Screwed or Slip-On

250

153 1.5

Blind

275 1.5

487 1.5

297 1.5

545 1.5

S.R. 90° Elbow

792 6

1315 6.3

922 6

1375 1680 2314 3610 6.3 6.5 6.9 7.3

L.R. 90° Elbow

1132 1725 1352 7.8 7.8 7.8

1705 7.8

45° Elbow

592 4.6

652 4.6

1105 1330 1917 2848 4.8 4.9 5.2 5.4

Tee

1178 2022 1378 9 9.5 9

1908 2370 3463 5520 9.5 9.7 10.1 11

Flanged Bonnet Gate

1934 3823 1855 8.3 9.5 6

3370 5700 5755 7 8 8

1055 4.8

2114 1.5

Flanged Bonnet – Globe or Angle Flanged Bonnet – Check

1772 11

800-899 4 24.6 4 37

900-999 1,000-1,099 1,100-1,200 4 41⁄2 41⁄2 24.6 28.1 28.1 4 41⁄2 41⁄2 37 43.1 43.1

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

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P IPING M ATERIALS – 24" P IPE (24" O.D.)

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt

5S 0.218 55.0

10 0.250 63.4

20/Std. 0.375 94.6

Water -- Lbs/Ft

188.9

188

183.8

PIPE XS 30 0.500 0.562 125.5 140.8

40 0.687 171.2

60 0.968 238.1

80 1.218 296.4

120 1.812 429.4

140 2.062 483.1

160 2.343 541.9

180.1

174.3

165.8

158.3

141.4

134.5

127.0

600-699 3 21.0 3 29.2

700-799 31⁄2 24.8 31⁄2 36.0

178.1

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

260.0 6.0

500.0 6.0

578.0 6.0

S.R. 90° Elbow

178.0 3.7

305.0 3.7

404.0 3.7

L.R. 45° Elbow

130.0 2.5

252.0 2.5

292.0 2.5

Tee

174.0 4.9

544.0 4.9

607.0 4.9

Lateral

361.0 10.0

544.0 10.0

875.0 10.0

Reducer

107.0 1.7

167.0 1.7

220.0 1.7

Cap

28.6 2.8

102.0 2.8

134.0 2.8

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 11⁄2 10.0

200-299 11⁄2 10.0

300-399 2 13.4

PIPE INSULATION 400-499 500-599 21⁄2 3 17.0 21.0

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

125

150

300

400

600

245 1.5

577 1.5

676 1.5

1056 1823 3378 1.5 1.5 1.5

Welding Neck

295 1.5

632 1.5

777 1.5

1157 2450 4153 1.5 1.5 1.5

Lap Joint

295 1.5

617 1.5

752 1.5

1046 2002 3478 1.5 1.5 1.5

446 1.5

841 1.5

1073 1355 2442 1.5 1.5 1.5

Screwed or Slip-On

250

236 1.5

Blind

404 1.5

S.R. 90° Elbow

1231 2014 1671 6.7 6.8 6.7

2174 2474 3506 6155 6.8 7.1 7.6 8.1

L.R. 90° Elbow

1711 2644 1821 8.7 8.7 8.7

2874 8.7

45° Elbow

871 4.8

1604 1121 5 4.8

1634 1974 2831 5124 5 5.1 5.5 6

Tee

1836 3061 2276 10 10.2 10

3161 3811 5184 9387 10.2 10.6 11.4 12.1

Flanged Bonnet Gate

3062 6484 2500 8.5 9.8 5

4675 6995 8020 7 8.7 9.5

Flanged Bonnet – Globe or Angle Flanged Bonnet – Check

2956 12

757 1.5

900 1500 2500

800-899 4 28.7 4 43.1

900-999 1,000-1,099 1,100-1,200 4 41⁄2 41⁄2 28.7 32.9 32.9 4 41⁄2 41⁄2 43.1 50.6 50.6

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

Pressure Seal – Bonnet, Gate Pressure Seal – Bonnet, Globe

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Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt Water -- Lbs/Ft

OF

P IPING M ATERIALS – 26" P IPE (26" O.D.)

0.250 67.0

10 0.312 85.7

PIPE Std. 20/XS 0.375 0.500 102.6 136.2

0.625 169.0

0.750 202.0

0.875 235.0

1.000 267.0

1.125 299.0

221.4

219.2

216.8

208.6

204.4

200.2

196.1

192.1

600-699 31⁄2 26.0 31⁄2 37.0

700-799 4 30.2 41⁄2 51.9

212.5

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

602.0 8.5

713.0 8.5

S.R. 90° Elbow

359.0 5.0

474.0 5.0

L.R. 45° Elbow

269.0 3.5

355.0 3.5

Tee

634.0 6.8

794.0 6.8

Reducer

200.0 2.5

272.0 2.5

Cap

110.0 4.3

145.0 4.3

Lateral

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 11⁄2 10.4

200-299 11⁄2 10.4

300-399 2 14.1

PIPE INSULATION 400-499 500-599 21⁄2 3 18.0 21.9

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

150

300

400

600

900 1500 2500

Screwed or Slip-On

125

250

292 1.5

699 1.5

650 1.5

950 1.5

1525 1.5

Welding Neck

342 1.5

799 1.5

750 1.5

1025 1575 1.5 1.5

567 1.5

1179 1125 1525 2200 1.5 1.5 1.5 1.5

Lap Joint Blind S.R. 90° Elbow L.R. 90° Elbow 45° Elbow Tee Flanged Bonnet Gate Flanged Bonnet – Globe or Angle Flanged Bonnet – Check

800-899 41⁄2 34.6 51⁄2 67.8

900-999 1,000-1,099 1,100-1,200 5 5 6 39.1 39.1 48.4 6 61⁄2 7 76.0 84.5 93.2

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

Pressure Seal – Bonnet, Gate Pressure Seal – Bonnet, Globe

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P IPING M ATERIALS – 28" P IPE (28" O.D.)

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt Water -- Lbs/Ft

0.250 74.0

10 0.312 92.4

PIPE Std. 20/XS 0.375 0.500 110.6 146.9

30 0.625 182.7

0.750 218.0

0.875 253.0

1.000 288.0

1.125 323.0

257.3

255.0

252.7

243.6

238.9

234.4

230.0

225.6

600-699 31⁄2 27.8 31⁄2 39.5

700-799 4 32.3 41⁄2 55.4

248.1

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

626.0 9.0

829.09 9.0

S.R. 90° Elbow

415.0 5.4

551.0 5.4

L.R. 45° Elbow

312.0 3.6

413.0 3.6

Tee

729.0 7.0

910.0 7.0

Reducer

210.0 2.7

290.0 2.7

Cap

120.0 4.5

160.0 4.5

Lateral

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 11⁄2 11.2

200-299 11⁄2 11.2

300-399 2 15.1

PIPE INSULATION 400-499 500-599 21⁄2 3 19.2 23.4

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

150

300

400

600

Screwed or Slip-On

125

250

334 1.5

853 1.5

780 1.5

1075 1800 1.5 1.5

900 1500 2500

Welding Neck

364 1.5

943 1.5

880 1.5

1175 1850 1.5 1.5

669 1.5

1408 1425 1750 2575 1.5 1.5 1.5 1.5

Lap Joint Blind S.R. 90° Elbow L.R. 90° Elbow 45° Elbow Tee Flanged Bonnet Gate Flanged Bonnet – Globe or Angle Flanged Bonnet – Check

800-899 41⁄2 36.9 51⁄2 72.2

900-999 1,000-1,099 1,100-1,200 5 5 6 41.6 41.6 51.4 6 61⁄2 7 80.9 89.8 99.0

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

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P IPING M ATERIALS – 30" P IPE (30" O.D.)

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt

PIPE 5S 10 & 10S Std. 20/XS 0.250 0.312 0.375 0.500 79.0 98.9 118.7 157.6

30 0.625 196.1

0.750 234.0

0.875 272.0

1.000 310.0

1.125 347.0

Water -- Lbs/Ft

296.3

281.1

276.6

271.8

267.0

262.2

600-699 31⁄2 29.5 31⁄2 42.1

700-799 4 34.3 41⁄2 58.9

293.5

291.0

286.0

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

478.0 10.0

775.0 10.0

953.0 10.0

596.0 10.0

S.R. 90° Elbow

319.0 5.9

470.0 5.9

644.0 5.9

388.0 5.9

L.R. 45° Elbow

239.0 3.9

358.0 3.9

475.0 3.9

298.0 3.9

855.0 7.8

1065.0 7.8

Reducer

220.0 3.9

315.0 3.9

Cap

125.0 4.8

175.0 4.8

Tee Lateral

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 11⁄2 11.9

200-299 11⁄2 11.9

300-399 2 16.1

PIPE INSULATION 400-499 500-599 21⁄2 3 20.5 25.0

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

150

300

400

600

Screwed or Slip-On

125

250

365 1.5

975 1.5

900 1.5

1175 2075 1.5 1.5

900 1500 2500

Welding Neck

410 1.5

1095 1000 1300 2150 1.5 1.5 1.5 1.5

770 1.5

1665 1675 2000 3025 1.5 1.5 1.5 1.5

Lap Joint Blind S.R. 90° Elbow L.R. 90° Elbow 45° Elbow Tee Flanged Bonnet Gate Flanged Bonnet – Globe or Angle Flanged Bonnet – Check

800-899 41⁄2 39.1 51⁄2 76.5

900-999 1,000-1,099 1,100-1,200 5 5 6 44.1 44.1 54.4 6 61⁄2 7 85.7 95.1 104.7

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

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P IPING M ATERIALS – 32" P IPE (32" O.D.)

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt Water -- Lbs/Ft

0.250 85.0

10 0.312 105.8

Std. 0.375 126.7

PIPE 20/XS 0.500 168.2

30 0.625 209.4

40 0.688 229.9

0.750 250.0

0.875 291.0

1.000 331.0

1.125 371.0

337.8

335.0

323.3

327.0

321.8

319.2

316.7

311.6

306.4

301.3

600-699 31⁄2 31.3 31⁄2 44.7

700-799 4 36.3 41⁄2 62.3

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

818.0 10.5

1090.0 10.5

S.R. 90° Elbow

546.0 6.3

722.0 6.3

L.R. 45° Elbow

408.0 4.2

541.0 4.2

Tee

991.0 8.4

1230.0 8.4

Reducer

255.0 3.1

335.0 3.1

Cap

145.0 5.2

190.0 5.2

Lateral

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 11⁄2 12.7

200-299 11⁄2 12.7

300-399 2 17.1

PIPE INSULATION 400-499 500-599 21⁄2 3 21.7 26.5

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

150

300

Screwed or Slip-On

125

250

476 1.5

1093 1025 1375 2500 1.5 1.5 1.5 1.5

400

600

900 1500 2500

Welding Neck

516 1.5

1228 1150 1500 2575 1.5 1.5 1.5 1.5

951 1.5

1978 1975 2300 3650 1.5 1.5 1.5 1.5

Lap Joint Blind S.R. 90° Elbow L.R. 90° Elbow 45° Elbow Tee Flanged Bonnet Gate Flanged Bonnet – Globe or Angle Flanged Bonnet – Check

800-899 41⁄2 41.4 51⁄2 80.9

900-999 1,000-1,099 1,100-1,200 5 5 6 46.6 46.6 57.5 6 61⁄2 7 90.5 100.4 110.5

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

Pressure Seal – Bonnet, Gate Pressure Seal – Bonnet, Globe

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Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt Water -- Lbs/Ft

OF

P IPING M ATERIALS – 34" P IPE (34" O.D.)

0.250 90.0

10 0.312 112.4

Std. 0.375 134.7

PIPE 20/XS 0.500 178.9

30 0.625 222.8

40 0.688 244.6

0.750 266.0

0.875 310.0

1.000 353.0

1.125 395.0

382.0

379.1

376.0

370.3

365.0

362.2

359.5

354.1

348.6

343.2

600-699 31⁄2 33.1 31⁄2 47.2

700-799 4 38.3 41⁄2 65.8

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

926.0 11.0

1230.0 11.0

S.R. 90° Elbow

617.0 5.5

817.0 5.5

L.R. 45° Elbow

463.0 4.4

615.0 4.4

Tee

1136.0 8.9

1420.0 8.9

Reducer

270.0 3.3

355.0 3.3

Cap

160.0 5.6

210.0 5.6

Lateral

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 11⁄2 13.4

200-299 11⁄2 13.4

300-399 2 18.2

PIPE INSULATION 400-499 500-599 21⁄2 3 23.0 28.0

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

150

300

Screwed or Slip-On

125

250

515 1.5

1281 1150 1500 2950 1.5 1.5 1.5 1.5

400

600

900 1500 2500

Welding Neck

560 1.5

1406 1300 1650 3025 1.5 1.5 1.5 1.5

1085 1.5

2231 2250 2575 4275 1.5 1.5 1.5 1.5

Lap Joint Blind S.R. 90° Elbow L.R. 90° Elbow 45° Elbow Tee Flanged Bonnet Gate Flanged Bonnet – Globe or Angle Flanged Bonnet – Check

800-899 41⁄2 43.7 51⁄2 85.3

900-999 1,000-1,099 1,100-1,200 5 5 6 49.1 49.1 60.5 6 61⁄2 7 95.4 105.7 116.3

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

Pressure Seal – Bonnet, Gate Pressure Seal – Bonnet, Globe

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P IPING M ATERIALS – 36" P IPE (36" O.D.)

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt Water -- Lbs/Ft

0.250 96.0

10 0.312 119.1

PIPE Std. 20/XS 0.375 0.500 142.7 189.6

30 0.625 236.1

40 0.750 282.4

0.875 328.0

1.000 374.0

1.125 419.0

429.1

425.9

422.6

411.0

405.1

399.4

393.6

387.9

600-699 31⁄2 34.8 31⁄2 49.8

700-799 4 40.3 41⁄2 69.3

416.6

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

1040.0 12.0

1380.0 12.0

S.R. 90° Elbow

692.0 5.0

913.0 5.0

L.R. 45° Elbow

518.0 4.8

686.0 4.8

Tee

1294.0 9.5

1610.0 9.5

Reducer

340.0 3.6

360.0 3.6

Cap

175.0 6.0

235.0 6.0

Lateral

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 11⁄2 14.2

200-299 11⁄2 14.2

300-399 2 19.2

PIPE INSULATION 400-499 500-599 21⁄2 3 24.2 29.5

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

150

300

Screwed or Slip-On

125

250

588 1.5

1485 1325 1600 3350 1.5 1.5 1.5 1.5

400

600

900 1500 2500

Welding Neck

628 1.5

1585 1475 1750 3450 1.5 1.5 1.5 1.5

1233 1.5

2560 2525 2950 4900 1.5 1.5 1.5 1.5

Lap Joint Blind S.R. 90° Elbow L.R. 90° Elbow 45° Elbow Tee Flanged Bonnet Gate Flanged Bonnet – Globe or Angle Flanged Bonnet – Check

800-899 41⁄2 45.9 51⁄2 89.7

900-999 1,000-1,099 1,100-1,200 5 5 6 51.7 51.7 63.5 6 61⁄2 7 100.2 111.0 122.0

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

Pressure Seal – Bonnet, Gate Pressure Seal – Bonnet, Globe

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61

W EIGHT

Sch./Wall Designation --> Thickness -- In. Pipe -- LbslFt Water -- Lbs/Ft

OF

P IPING M ATERIALS – 42" P IPE (42" O.D.)

0.250 112.0

Std. 0.375 166.7

PIPE 20/XS 0.500 221.6

30 0.625 276.0

40 0.750 330.0

1.000 438.0

1.250 544.0

1.500 649.0

586.4

578.7

571.7

565.4

558.4

544.8

531.2

517.9

600-699 31⁄2 40.1 31⁄2 57.4

700-799 4 46.4 41⁄2 79.7

WELDED FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR L.R. 90° Elbow

1420.0 15.0

1880.0 15.0

S.R. 90° Elbow

1079.0 9.0

1430.0 9.0

L.R. 45° Elbow

707.0 6.0

937.0 6.0

Tee

1870.0

2415.0

Reducer

310.0 4.5

410.0 4.5

Cap

230.0 7.5

300.0 7.5

Lateral

Temp. Range --> 85% Magnesia Calcium Silicate Combination

Nom. Thick., In. Lbs./Ft Nom. Thick., In. Lbs/Ft

100-199 11⁄2 16.5

200-299 11⁄2 16.5

300-399 2 22.2

PIPE INSULATION 400-499 500-599 21⁄2 3 28.0 34.0

CAST IRON & STEEL FITTINGS - LINE 1: WEIGHT IN POUNDS, LINE 2: INSULATION WEIGHT FACTOR Pressure Rating (PSI) Cast Iron ––––––––––––––––– Steel –––––––––––––

150

300

Screwed or Slip-On

125

250

792 1.5

1895 1759 2320 1.5 1.5 1.5

400

600

Welding Neck

862 1.5

2024 1879 2414 1.5 1.5 1.5

1733 1.5

3449 3576 4419 1.5 1.5 1.5

900 1500 2500

Lap Joint Blind S.R. 90° Elbow L.R. 90° Elbow 45° Elbow Tee Flanged Bonnet Gate Flanged Bonnet – Globe or Angle Flanged Bonnet – Check

800-899 41⁄2 52.7 51⁄2 102.8

900-999 1,000-1,099 1,100-1,200 5 5 6 59.2 59.2 72.6 6 61⁄2 7 114.8 126.9 139.3

Note: Boldface type is weight in pounds and light type underneath is weight factor for insulation. • Insulation thicknesses and weights are based on average conditions and do not constitute a recommendation for specific thicknesses of materials. • Insulation weights are based on 85% magnesia and hydrous calcium silicate at 11 Ibs/cu. foot. The listed thicknesses and weights of combination covering are the sums of the inner layer of diatomaceous earth at 21 Ibs/cu. foot and the outer layer at 11 Ibs/ cubic foot. • Insulation weights include allowances for wire, cement, canvas, bands and paint but not special surface finishes. • To find the weight of covering on flanges, valves or fittings, multiply the weight factor by the weight per foot of covering used on straight pipe. • Valve weights are approximate. Whenever possible, obtain weights from the manufacturer. • Cast iron valve weights are for flanged end valves; steel weights for welding end valves. • All flanged fitting, flanged valve and flange weights include the proportional weight of bolts or studs to make up all joints.

Pressure Seal – Bonnet, Gate Pressure Seal – Bonnet, Globe

62

Anvil International, Piping & Pipe Hanger Design and Engineering

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T HERMAL E XPANSION

OF

P IPE M ATERIALS THERMAL EXPANSION OF PIPE MATERIALS – INCHES PER FOOT

Carbon Steel • Carbon Moly Steel • Low-Chrome Steel (Thru 3% Cr) –– Temperature 10 20 30 40 50 60 70

Temp °F

O

80

90

-200

-0.0180

-0.0187

-0.0192

-0.0198

-0.0203

-0.0209

-0.0215

-0.0220

-0.0225

-0.0230

-100

-0.0121

-0.0127

-0.0133

-0.0140

-0.0146

-0.0152

-0.0158

-0.0163

-0.0169

-0.0171

-0

-0.0051

-0.0058

-0.0065

-0.0073

-0.0080

-0.0087

-0.0096

-0.0103

-0.0109

-0.0116

0

-0.0051

-0.0044

-0.0037

-0.0029

-0.0022

-0.0015

-0.0007

0.0000

0.0008

0.0015

100

0.0023

0.0030

0.0038

0.0046

0.0053

0.0061

0.0068

0.0076

0.0084

0.0091

200

0.0099

0.0107

0.0116

0.0124

0.0132

0.0141

0.0149

0.0157

0.0165

0.0174

300

0.0182

400

0.0270

0.0191

0.0200

0.0208

0.0217

0.0226

0.0235

0.0244

0.0252

0.0261

0.0279

0.0288

0.0298

0.0307

0.0316

0.0325

0.0344

0.0344

0.0353

500

0.0362

0.0372

0.0382

0.0391

0.0401

0.0411

0.0421

0.0431

0.0440

0.0450

600

0.0460

0.0470

0.0481

0.0491

0.0501

0.0512

0.0522

0.0532

0.0542

0.0553

700

0.0563

0.0574

0.0584

0.0595

0.0606

0.0617

0.0627

0.0638

0.0649

0.0659

800

0.0670

0.0681

0.0692

0.0703

0.0714

0.0726

0.0737

0.0748

0.0759

0.0770

900

0.0781

0.0792

0.0803

0.0813

0.0824

0.0835

0.0846

0.0857

0.0867

0.0878

1,000

0.0889

0.0901

0.0912

0.0924

0.9350

0.0946

0.0958

0.0970

0.0981

0.3993

1,100

0.1004

0.1015

0.1025

0.1036

0.1046

0.1057

0.1068

0.1078

0.1089

0.1099

1,200

0.1110

0.1121

0.1132

0.1144

0.1155

0.1166

0.1177

0.1188

0.1200

0.1211

1,300

0.1222

0.1233

0.1244

0.1256

0.1267

0.1278

0.1299

0.1320

0.1342

0.1363

1,400

0.1334

0.0000

0.0000

0.0000

0.0000

0.0000

0.0000

0.0000

0.0000

0.0000

70

80

90

THERMAL EXPANSION OF PIPE MATERIALS – INCHES PER FOOT Austenitic Stainless Steels (304, 316, 347) –– Temperature 20 30 40 50 60

Temp °F

O

10

-200

-0.0281

-0.0295

-0.0305

-0.0314

-0.0324

-0.0334

-0.0343

-0.0353

-0.0362

-0.0372

-100

-0.0187

-0.0197

-0.0207

-0.0216

-0.0226

-0.0236

-0.0245

-0.0254

-0.0263

-0.0272

-0

-0.0078

-0.0089

-0.0100

-0.0112

-0.0123

-0.0134

-0.0145

-0.0155

-0.0166

-0.0176

0

-0.0078

-0.0067

-0.0056

-0.0044

-0.0033

-0.0022

-0.0011

0.0000

0.0012

0.0023

100

0.0034

0.0045

0.0056

0.0068

0.0079

0.0090

0.0101

0.0112

0.0124

0.0135

200

0.0146

0.0158

0.0169

0.0181

0.0192

0.0203

0.0215

0.0227

0.0238

0.0250

300

0.0261

0.0273

0.0285

0.0297

0.0309

0.0321

0.0332

0.0344

0.0356

0.0368

400

0.0380

0.0392

0.0404

0.0416

0.0428

0.0440

0.0453

0.0465

0.0477

0.0489

500

0.0501

0.0513

0.0526

0.0538

0.0550

0.0562

0.0575

0.0587

0.0599

0.0612

600

0.0624

0.0637

0.0649

0.0662

0.0674

0.0687

0.0700

0.0712

0.0725

0.0737

700

0.0750

0.0763

0.0776

0.0789

0.0802

0.0815

0.0828

0.0841

0.0854

0.0867

800

0.0880

0.0893

0.0906

0.0920

0.0933

0.0946

0.0959

0.0972

0.0986

0.0999

900

0.1012

0.1026

0.1039

0.1053

0.1066

0.1080

0.1094

0.1107

0.1121

0.1134

1,000

0.1148

0.1162

0.1175

0.1189

0.1202

0.1216

0.1229

0.1243

0.1257

0.1270

1,100

0.1284

0.1298

0.1311

0.1325

0.1338

0.1352

0.1366

0.1379

0.1393

0.1406

1,200

0.1420

0.1434

0.1447

0.1461

0.1474

0.1488

0.1502

0.1515

0.1529

0.1542

1,300

0.1556

0.1570

0.1583

0.1597

0.1610

0.1624

0.1638

0.1651

0.1665

0.1678

1,400

0.1692

0.1704

0.1717

0.1731

0.1744

0.1757

0.1771

0.1784

0.1796

0.1811

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63

T HERMAL E XPANSION THERMAL EXPANSION OF PIPE MATERIALS – INCHES PER FOOT Temp. °F

-200

64

Intermediate Alloy Steels (5% thru 9% Cr Mo)

–

Copper

Brass

-0.2870

P IPE M ATERIALS

PROPERTIES OF SATURATED STEAM

Aluminum

(STANDARD BAROMETER 14,696 PSI) Guage

Pressure -0.0275

OF

-0.0373

Temperature

Lbs./Sq. In.

°F

0

212.00

5

227.14

10

239.39

15

249.75

-150

–

-0.0231

-0.0241

-0.0310

-100

–

-0.1830

-0.1900

-0.0244

-50

–

-0.1320

-0.0137

-0.0176

0

–

-0.0790

-0.0081

-0.0104

20

258.76

50

–

-0.0022

-0.0023

-0.0030

25

266.78

70

0.0000

0.0000

0.0000

0.0000

30

274.02

100

0.0022

0.0034

0.0035

0.0046

35

280.62

150

0.0058

0.0091

0.0093

0.0123

40

286.71

200

0.0094

0.0151

0.0152

0.0200

45

292.37

50

297.66

55

302.62

60

307.32

65

311.77

70

316.00

75

320.03

250

0.0132

0.0208

0.0214

0.0283

300

0.0171

0.0267

0.0276

0.0366

350

0.0210

0.0327

0.0340

0.0452

400

0.0250

0.0388

0.0405

0.0539

450

0.0292

0.0449

0.0472

0.0628

500

0.0335

0.0512

0.0540

0.0717

80

323.90

550

0.0379

0.0574

0.0610

0.0810

85

327.59

600

0.0424

0.0639

0.0680

0.0903

90

331.15

650

0.0469

0.0703

0.0753

–

95

334.57 337.88

700

0.0514

0.0768

0.0826

–

100

750

0.0562

0.0834

0.0902

–

150

365.85

800

0.0610

0.0900

0.0978

–

200

387.78

250

406.01

300

421.71

350

435.59

850

0.0658

0.0967

0.1056

–

900

0.0707

0.1037

0.1135

–

950

0.0756

0.1105

0.1216

–

400

448.12

1000

0.0806

0.1175

0.1298

–

450

459.59

1050

0.0855

–

–

–

500

469.99

1100

0.0905

–

–

–

550

479.93 488.79

1150

0.0952

–

–

–

600

1200

0.1000

–

–

–

650

497.29

1250

0.1053

–

–

–

700

505.15

750

512.75

800

520.92

850

526.97

900

533.63

1300

0.1106

–

–

–

1350

0.1155

–

–

–

1400

0.1205

–

–

–

Anvil International, Piping & Pipe Hanger Design and Engineering

950

540.26

1000

546.12

1050

551.98

1100

557.84

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D EFLECTION

OF

E MPTY P IPE

24" 20" 18" 16" 14" 12"

SPAN-FEET

Deflection of Empty Pipe, Standard Weight, Caused by Load Between Supports, Based on Single Span with Free Ends

∆=

5wl4 384 EI

10"

w = weight in pounds per linear inch l = distance between hangers in inches E = modulus of elasticity I = moment of inertia

8" 6"

▲

5"

50

4" 31⁄2" 3"

40

21⁄2" 2" 30

11⁄2" 11⁄4" 1"

▲

in 5

'

0'

1"

in 1 1"

in 1

5'

0' 1"

in 2 1"

1"

in 3

0'

0' in 4

0'

1"

in 5

1"

in 6

0'

0' 1"

in 8

Nominal Pipe Size

15

1"

1"

in 1

00'

20

10 9 8 7

6 0.02

0.03

0.04

0.05 0.06

0.08

0.1

0.2

0.3

0.4

0.5

0.6

0.8

1.0

2.0

3.0

4.0

5.0

DEFLECTION - INCHES

Values are plotted for the pipes empty since this more nearly approaches the condition that exists for pocketing of condensation. Although the weight of fluid carried by the pipe will cause an increase in the deflection of the pipe between supports, this increased sag disappears during drainage. Therefore, the deflection produced by the weight of empty pipe should be considered in determining slope for drainage. This chart is based on E = 29,000,000 P.S.I.

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65

B ENDING S TRESS

90 80

E MPTY P IPE

Bending Stress in Empty Pipe, Standard Weight, Caused by Load Between Supports –– Based on Single Span with Free Ends. 2 S= w l

70

60

IN

8 Sm

w = weight in pounds per linear inch l = distance between hangers in inches Sm = section modulus

50

24 20 " 18 " 16 " "

40

"

14

12

"

30 "

10

8"

▲

SPAN-FEET

6"

Nominal Pipe Size

20

5"

4"

1 ⁄2

3

15 3"

"

"

1 ⁄2

2

2" 1 ⁄2

1

" 1 ⁄4

1

1"

"

10 9 8 7

6

5

50,000

40,000

30,000

20,000

8000 9000 10000

7000

6000

5000

4000

3000

2000

700

600

500

400

300

200

3

800 900 1000

4

MAXIMUM BENDING STRESS –– P.S.I.

66

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B ENDING S TRESS

90 80

IN

W ATER F ILLED P IPE

Bending Stress in Water Filled Pipe, Standard Weight, Caused by Load Between Supports –– Based on Single Span with Free Ends.

S=

70

wl2 8 Sm

w = weight in pounds per linear inch l = distance between hangers in inches Sm = section modulus

60

50

40

SPAN-FEET

24 16 " "

30

20

▲

Nominal Pipe Size

"

10

8"

6"

5"

4"

15 " 3"

1 ⁄2

3

"

1 ⁄2

2 2"

10

"

1 ⁄2

1 "

1 ⁄4

1

9 1"

8 7

6

5

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Anvil International, Piping & Pipe Hanger Design and Engineering

50,000

40,000

30,000

MAXIMUM BENDING STRESS –– P.S.I.

20,000

8000 9000 10,000

7000

6000

5000

4000

3000

2000

700

600

500

400

300

200

3

800 900 1000

4

67

M INIMUM D ISTANCE

TO

F IRST H ANGER

MINIMUM DISTANCE TO FIRST RIGID HANGER

L=

∆ x (O.D. of Pipe) x 106 1.6 x S

S = 10,000 p.s.i

Pipe Size, Pipe O.D. 1 1.315

11⁄4 1.660

11⁄2 1.900

2 2.375

21⁄2 2.875

3 3.5

31⁄2 4

4 4.5

5 5.563

6 6.625

8 8.625

10 10.75

12 12.75

14 14

16 16

18 18

20 20

1

41⁄2

5

51⁄2

6

61⁄2

71⁄2

8

81⁄2

91⁄2

10

111⁄2

13

14

15

16

17

171⁄2

1

61⁄2

7

71⁄2

81⁄2

91⁄2

101⁄2

11

12

13

141⁄2

161⁄2

181⁄2

20

21

221⁄2

231⁄2

25

3

⁄4

8

9

91⁄2

101⁄2

111⁄2

13

131⁄2

141⁄2

16

171⁄2

20

221⁄2

241⁄2

251⁄2

271⁄2

29

301⁄2

1

9

10

11

12

131⁄2

15

16

17

181⁄2

201⁄2

23

26

28

291⁄2

311⁄2

331⁄2

351⁄2

11⁄4

10

111⁄2

12

131⁄2

15

161⁄2

171⁄2

19

21

23

26

29

311⁄2

33

351⁄2

371⁄2

391⁄2

11⁄2

11

121⁄2

131⁄2

15

161⁄2

18

191⁄2

201⁄2

23

25

281⁄2

311⁄2

341⁄2

36

381⁄2

41

431⁄2

13⁄4

12

131⁄2

141⁄2

16

171⁄2

191⁄2

21

22

241⁄2

27

301⁄2

341⁄2

371⁄2

39

42

441⁄2

47

2

13

141⁄2

151⁄2

17

19

21

221⁄2

231⁄2

261⁄2

29

33

361⁄2

40

42

441⁄2

471⁄2

50

21⁄4

131⁄2

151⁄2

161⁄2

181⁄2

20

22

231⁄2

25

28

301⁄2

35

39

421⁄2

441⁄2

471⁄2

501⁄2

53

21⁄2

141⁄2

16

17

191⁄2

21

231⁄2

25

261⁄2

291⁄2

32

361⁄2

41

441⁄2

47

50

53

56

23⁄4

15

17

18

20

22

241⁄2

26

28

31

331⁄2

381⁄2

43

47

49

521⁄2

551⁄2

581⁄2

3

151⁄2

171⁄2

19

21

23

251⁄2

271⁄2

29

321⁄2

35

40

45

49

51

55

58

61

31⁄2

17

19

201⁄2

23

25

271⁄2

291⁄2

311⁄2

35

38

431⁄2

481⁄2

53

551⁄2

59

621⁄2

66

4

18

201⁄2

22

241⁄2

27

291⁄2

311⁄2

331⁄2

371⁄2

401⁄2

461⁄2

52

561⁄2

59

63

67

701⁄2

41⁄2

19

211⁄2

23

26

281⁄2

311⁄2

331⁄2

351⁄2

391⁄2

43

491⁄2

55

60

621⁄2

67

71

75

5

201⁄2

23

241⁄2

27

30

33

351⁄2

371⁄2

411⁄2

451⁄2

52

58

63

66

701⁄2

75

79

51⁄2

211⁄2

24

251⁄2

281⁄2

311⁄2

341⁄2

37

391⁄2

431⁄2

471⁄2

541⁄2

61

66

691⁄2

74

781⁄2

83

6

22

25

261⁄2

30

33

36

381⁄2

41

451⁄2

50

57

631⁄2

69

721⁄2

771⁄2

82

861⁄2

⁄4

Deflection

⁄2

68

Anvil International, Piping & Pipe Hanger Design and Engineering

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B EAM D IMENSIONS AMERICAN STANDARD CHANNELS Y (Depth of Section)

3

4 5

6

7

8

9

10

12

15

18

Wt./Ft. Ib

Width in

4.1

13⁄8

5.0

1

1 ⁄2

6.0

15⁄8

5.4

15⁄8

7.25

13⁄4

6.7

13⁄4

9.0

7

1 ⁄8

8.2

17⁄8

10.5

2

13.0

1

2 ⁄8

9.8

21⁄8

12.15

1

2 ⁄4

14.75

23⁄8

11.5

21⁄4

13.75

21⁄4

18.75

1

2 ⁄2

13.4

23⁄8

15.0

21⁄2

20.0

25⁄8

15.3

5

20.0 25.0

27⁄8

30.0

3

20.7

3

25.0

3

30.0

31⁄8 3

W SHAPES

Y (Depth of Section)

Y (Depth of Section)

Wt./Ft. Ib

Width in

5.7

23⁄8

7.5

21⁄2

7.7

25⁄8

9.5

23⁄4

10.0

3

14.75

31⁄4

12.5

33⁄8

12.25

35⁄8

15.3

35⁄8

20.0

37⁄8

18.4

4

23.0

41⁄8

25.4

45⁄8

35.0

5

31.8

5

35.0

51⁄8

40.8

51⁄4

50.0

51⁄2

42.9

51⁄2

2 ⁄8

50.0

5

23⁄4

54.7

6

70.0

61⁄4

66.0

61⁄4

75.5

63⁄8

86.0

7

96.0

71⁄4

33.9

3 ⁄8

40.0

31⁄2

50.0

33⁄4

42.7

4

45.8

4

51.9

41⁄8

58.0

41⁄4

Z (Mean Thickness of Flange)

Z (Mean Thickness of Flange)

Z (Mean Thickness of Flange)

Y in

S SHAPES

Z in

Y in 3

0.250 4 0.313 5 0.313 6 0.375

7 8

0.375 10 0.375 12 0.438 15

0.438

18 20

0.500 20.3

0.625

24

Z in 0.250

Y in 5 6

0.313 0.313 8 0.375 0.375 0.438 0.500 0.563

10

0.688 0.625

5 ⁄8

80.0

7

90.0

71⁄8

100.0

71⁄4

0.688 0.813 0.938 12 0.875

0.625

14

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Wt./Ft. Ib 19.0 25.0 18.0 21.0 24.0 28.0 31.0 35.0 40.0 48.0 58.0 67.0 22.0 26.0 30.0 33.0 39.0 45.0 49.0 54.0 60.0 68.0 77.0 88.0 26.0 30.0 35.0 40.0 45.0 50.0 53.0 58.0 65.0 72.0 79.0 87.0 96.0 106.0 30.0 34.0 38.0 43.0 48.0 53.0 61.0 68.0 74.0 82.0 90.0 99.0 109.0 120.0 132.0

Width in 5 61⁄8 51⁄4 51⁄4 61⁄2 61⁄2 8 8 81⁄8 81⁄8 81⁄4 81⁄4 53⁄4 53⁄4 53⁄4 8 8 8 10 10 101⁄8 101⁄8 101⁄4 101⁄4 61⁄2 61⁄2 61⁄2 8 8 81⁄8 10 10 12 12 121⁄8 121⁄8 121⁄8 121⁄4 63⁄4 63⁄4 63⁄4 8 8 8 10 10 101⁄8 101⁄8 141⁄2 145⁄8 145⁄8 145⁄8 143⁄4

Z in 0.430 0.455 0.330 0.400 0.400 0.465 0.435 0.495 0.560 0.685 0.810 0.935 0.360 0.440 0.510 0.435 0.530 0.620 0.560 0.615 0.680 0.770 0.870 0.990 0.380 0.440 0.520 0.515 0.575 0.640 0.575 0.640 0.605 0.670 0.735 0.810 0.900 0.990 0.385 0.455 0.515 0.530 0.595 0.660 0.645 0.720 0.785 0.855 0.710 0.780 0.860 0.940 1.030

Y in

16

18

21

24

27

30

33

36

Wt./Ft. Ib 36.0 40.0 45.0 50.0 57.0 67.0 77.0 89.0 100.0 50.0 55.0 60.0 65.0 71.0 76.0 86.0 97.0 106.0 62.0 68.0 73.0 83.0 93.0 101.0 111.0 122.0 76.0 84.0 94.0 104.0 117.0 131.0 94.0 102.0 114.0 146.0 108.0 116.0 124.0 132.0 118.0 130.0 141.0 135.0 150.0 160.0

Width in 7 7 7 71⁄8 71⁄8 101⁄4 101⁄4 103⁄8 103⁄8 71⁄2 71⁄2 71⁄2 75⁄8 75⁄8 11 111⁄8 111⁄8 111⁄4 81⁄4 81⁄4 81⁄4 83⁄8 83⁄8 121⁄4 123⁄8 123⁄8 9 9 91⁄8 123⁄4 123⁄4 127⁄8 10 10 101⁄8 14 101⁄2 101⁄2 101⁄2 101⁄2 111⁄2 111⁄2 111⁄2 12 12 12

Anvil International, Piping & Pipe Hanger Design and Engineering

Z in 0.430 0.505 0.565 0.630 0.715 0.665 0.760 0.875 0.985 0.570 0.630 0.695 0.750 0.810 0.680 0.770 0.870 0.940 0.615 0.685 0.740 0.835 0.930 0.800 0.875 0.960 0.680 0.770 0.875 0.750 0.850 0.960 0.745 0.830 0.930 0.975 0.760 0.850 0.930 1.000 0.740 0.855 0.960 0.790 0.940 1.020

69

F ORCE B ASED

ON

S PAN

100 90 80

▲

70

Nominal Pipe Size

60

50

40

30 20"

18" 16"

12"

14"

10"

20 8"

6"

2" "

8

11 ⁄2

9 " 11 ⁄4

SPAN-FEET

5"

4"

" 31 ⁄2 3" " 21 ⁄2

10

1"

7 6 5

4

*P= S

3

Sm 6L

Force "P" Based on Spans (L) Obtained in Chart on Page 66 and SCH 40 Pipe for Other Schedules of Pipe. Multiply "P" by the Ratio of the

2

Section Modulus (Sm ) of the New Schedule Pipe to the Section Modulus of SCH 40 Pipe.

20,000

6000 7000 8000 9000 10,000

5000

4000

3000

2000

600 700 800 900 1000

500

400

300

200

60 70 80 90 100

50

40

30

20

10

*Based on guided cantilever

Force –– lbs.

70

Anvil International, Piping & Pipe Hanger Design and Engineering

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T EMPERATURE C ONVERSIONS TEMPERATURE CONVERSIONS To convert C° to F°, find C° value in the middle column and read F° in right hand column. To convert F° to C°, find F° value in the middle column and read C° in left hand column. F to C Input C to F

F to C Input C to F

F to C Input C to F

-273 -459.4 -268 -450 -262 -440 -257 -430

– – – –

-8.3 -7.8 -7.2 -6.7

17 18 19 20

62.6 64.4 66.2 68.0

27.2 27.8 28.3 28.9

81 82 83 84

177.8 179.6 181.4 183.2

282 288 293 299

540 550 560 570

1,004 1,022 1,040 1,058

638 643 649 654

1,180 1,190 1,200 1,210

2,156 2,174 2,192 2,210

993 999 1,004 1,010

1,820 1,830 1,840 1,850

3,308 3,326 3,344 3,362

1,349 1,354 1,360 1,366

2,460 2,470 2,480 2,490

4,460 4,478 4,496 4,514

-251 -246 -240 -234

-420 -410 -400 -390

– – – –

-6.1 -5.6 -5.0 -4.4

21 22 23 24

69.8 71.6 73.4 75.2

29.4 30.0 30.6 31.1

85 86 87 88

185.0 186.8 188.6 190.4

304 310 316 321

580 590 600 610

1,076 1,094 1,112 1,130

660 666 671 677

1,220 1,230 1,240 1,250

2,228 2,246 2,264 2,282

1,016 1,021 1,027 1,032

1,860 1,870 1,880 1,890

3,380 3,398 3,416 3,434

1,371 1,377 1,382 1,388

2,500 2,510 2,520 2,530

4,532 4,550 4,568 4,586

-229 -223 -218 -212

-380 -370 -360 -350

– – – –

-3.9 -3.3 -2.8 -2.2

25 26 27 28

77.0 78.8 80.6 82.4

31.7 32.2 32.8 33.3

89 90 91 92

192.2 194.0 195.8 197.6

327 332 338 343

620 630 640 650

1,148 1,166 1,184 1,202

682 688 693 699

1,260 1,270 1,280 1,290

2,300 2,318 2,336 2,354

1,038 1,043 1,049 1,054

1,900 1,910 1,920 1,930

3,452 3,470 3,488 3,506

1,393 1,399 1,404 1,410

2,540 2,550 2,560 2,570

4,604 4,622 4,640 4,658

-207 -201 -196 -190

-340 -330 -320 -310

– – – –

-1.7 -1.1 -0.6 0.0

29 30 31 32

84.2 86.0 87.8 89.6

33.9 34.4 35.0 35.6

93 94 95 96

199.4 201.2 203.0 204.8

349 354 360 366

660 670 680 690

1,220 1,238 1,256 1,274

704 710 716 721

1,300 1,310 1,320 1,330

2,372 2,390 2,408 2,426

1,060 1,066 1,071 1,077

1,940 1,950 1,960 1,970

3,524 3,542 3,560 3,578

1,416 1,421 1,427 1,432

2,580 2,590 2,600 2,610

4,676 4,694 4,712 4,730

-184 -179 -173 -169

-300 – -290 – -280 – -273 -459.4

0.6 1.1 1.7 2.2

33 34 35 36

91.4 93.2 95.0 96.8

36.1 36.7 37.2 37.8

97 98 99 100

206.6 208.4 210.2 212.0

371 377 382 388

700 710 720 730

1,292 1,310 1,328 1,346

727 732 738 743

1,340 1,350 1,360 1,370

2,444 2,462 2,480 2,498

1,082 1,088 1,093 1,099

1,980 1,990 2,000 2,010

3,596 3,614 3,632 3,650

1,438 1,443 1,449 1,454

2,620 2,630 2,640 2,650

4,748 4,766 4,784 4,802

-168 -162 -157 -151

-270 -260 -250 -240

-454.0 -436.0 -418.0 -400.0

2.8 3.3 3.9 4.4

37 38 39 40

98.6 100.4 102.2 104.0

43.3 48.9 54.4 60.0

110 120 130 140

230.0 248.0 266.0 284.0

393 399 404 410

740 750 760 770

1,364 1,382 1,400 1,418

749 754 760 766

1,380 1,390 1,400 1,410

2,516 2,534 2,552 2,570

1,104 1,110 1,116 1,121

2,020 2,030 2,040 2,050

3,668 3,686 3,704 3,722

1,460 1,466 1,471 1,477

2,660 2,670 2,680 2,690

4,820 4,838 4,856 4,874

-146 -140 -134 -129

-230 -220 -210 -200

-382.0 -364.0 -346.0 -328.0

5.0 5.6 6.1 6.7

41 42 43 44

105.8 107.6 109.4 111.2

65.6 71.1 76.7 82.2

150 160 170 180

302.0 320.0 338.0 356.0

416 421 427 432

780 790 800 810

1,436 1,454 1,472 1,490

771 777 782 788

1,420 1,430 1,440 1,450

2,588 2,606 2,624 2,642

1,127 1,132 1,138 1,143

2,060 2,070 2,080 2,090

3,740 3,758 3,776 3,794

1,482 1,488 1,493 1,499

2,700 2,710 2,720 2,730

4,892 4,910 4,928 4,946

-123 -118 -112 -107

-190 -180 -170 -160

-310.0 -292.0 -274.0 -256.0

7.2 7.8 8.3 8.9

45 46 47 48

113.0 114.8 116.6 118.4

87.8 93.3 98.9 100

190 200 210 212

374.0 392.0 410.0 413.6

438 443 449 454

820 830 840 850

1,508 1,526 1,544 1,562

793 799 804 810

1,460 1,470 1,480 1,490

2,660 2,678 2,696 2,714

1,149 1,154 1,160 1,166

2,100 2,110 2,120 2,130

3,812 3,830 3,848 3,866

1,504 1,510 1,516 1,521

2,740 2,750 2,760 2,770

4,964 4,982 5,000 5,018

-101 -96 -90 -84

-150 -140 -130 -120

-238.0 -220.0 -202.0 -184.0

9.4 10.0 10.6 11.1

49 50 51 52

120.2 122.0 123.8 125.6

104 110 116 121

220 230 240 250

428.0 446.0 464.0 482.0

460 466 471 477

860 870 880 890

1,580 1,598 1,616 1,634

816 821 827 832

1,500 1,510 1,520 1,530

2,732 2,750 2,768 2,786

1,171 1,177 1,182 1,188

2,140 2,150 2,160 2,170

3,884 3,902 3,920 3,938

1,527 1,532 1,538 1,543

2,780 2,790 2,800 2,810

5,036 5,054 5,072 5,090

-79 -73 -68 -62

-110 -100 -90 -80

-166.0 -148.0 -130.0 -112.0

11.7 12.2 12.8 13.3

53 54 55 56

127.4 129.2 131.0 132.8

127 132 138 143

260 270 280 290

500.0 518.0 536.0 554.0

482 488 493 499

900 910 920 930

1,652 1,670 1,688 1,706

838 843 849 854

1,540 1,550 1,560 1,570

2,804 2,822 2,840 2,858

1,193 1,199 1,204 1,210

2,180 2,190 2,200 2,210

3,956 3,974 3,992 4,010

1,549 1,554 1,560 1,566

2,820 2,830 2,840 2,850

5,108 5,126 5,144 5,162

-57 -51 -46 -40

-70 -60 -50 -40

-94.0 -76.0 -58.0 -40.0

13.9 14.4 15.0 15.6

57 58 59 60

134.6 136.4 138.2 140.0

149 154 160 166

300 310 320 330

572.0 590.0 608.0 626.0

504 510 516 521

940 950 960 970

1,724 1,742 1,760 1,778

860 866 871 877

1,580 1,590 1,600 1,610

2,876 2,894 2,912 2,930

1,216 1,221 1,227 1,232

2,220 2,230 2,240 2,250

4,028 4,046 4,064 4,082

1,571 1,577 1,582 1,588

2,860 2,870 2,880 2,890

5,180 5,198 5,216 5,234

-34 -29 -23 -17.8

-30 -20 -10 0

-22.0 -4.0 14.0 32.0

16.1 16.7 17.2 17.8

61 62 63 64

141.8 143.6 145.4 147.2

171 177 182 188

340 350 360 370

644.0 662.0 680.0 698.0

527 532 538 543

980 990 1,000 1,010

1,796 1,814 1,832 1,850

882 888 893 899

1,620 1,630 1,640 1,650

2,948 2,966 2,984 3,002

1,238 1,243 1,249 1,254

2,260 2,270 2,280 2,290

4,100 4,118 4,136 4,154

1,593 1,599 1,604 1,610

2,900 2,910 2,920 2,930

5,252 5,270 5,288 5,306

-17.2 -16.7 -16.1 -15.6

1 2 3 4

33.8 35.6 37.4 39.2

18.3 18.9 19.4 20.0

65 66 67 68

149.0 150.8 152.6 154.4

193 199 204 210

380 390 400 410

716.0 734.0 752.0 770.0

549 554 560 566

1,020 1,030 1,040 1,050

1,868 1,886 1,904 1,922

904 910 916 921

1,660 1,670 1,680 1,690

3,020 3,038 3,056 3,074

1,260 1,266 1,271 1,277

2,300 2,310 2,320 2,330

4,172 4,190 4,208 4,226

1,616 1,621 1,627 1,632

2,940 2,950 2,960 2,970

5,324 5,342 5,360 5,378

-15.0 -14.4 -13.9 -13.3

5 6 7 8

41.0 42.8 44.6 46.4

20.6 21.1 21.7 22.2

69 70 71 72

156.2 158.0 159.8 161.6

216 221 227 232

420 430 440 450

788.0 806.0 824.0 842.0

571 577 582 588

1,060 1,070 1,080 1,090

1,940 1,958 1,976 1,994

927 932 938 943

1,700 1,710 1,720 1,730

3,092 3,110 3,128 3,146

1,282 1,288 1,293 1,299

2,340 2,350 2,360 2,370

4,244 4,262 4,280 4,298

1,638 2,980 5,396 1,643 2,990 5,414 1,649 3,000 5,432

-12.8 -12.2 -11.7 -11.1

9 10 11 12

48.2 50.0 51.8 53.6

22.8 23.3 23.9 24.4

73 74 75 76

163.4 165.2 167.0 168.8

238 243 249 254

460 470 480 490

860.0 878.0 896.0 914.0

593 599 604 610

1,100 1,110 1,120 1,130

2,012 2,030 2,048 2,066

949 954 960 966

1,740 1,750 1,760 1,770

3,164 3,182 3,200 3,218

1,304 1,310 1,316 1,321

2,380 2,390 2,400 2,410

4,316 4,334 4,352 4,370

-10.6 -10.0 -9.4 -8.9

13 14 15 16

55.4 57.2 59.0 60.8

25.0 25.6 26.1 26.7

77 78 79 80

170.6 172.4 174.2 176.0

260 266 271 277

500 510 520 530

932.0 950.0 968.0 986.0

616 621 627 632

1,140 1,150 1,160 1,170

2,084 2,102 2,120 2,138

971 977 982 988

1,780 1,790 1,800 1,810

3,236 3,254 3,272 3,290

1,327 1,332 1,338 1,343

2,420 2,430 2,440 2,450

4,388 4,406 4,424 4,442

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F to C Input C to F

F to C Input C to F

F to C Input C to F

F to C Input C to F

Anvil International, Piping & Pipe Hanger Design and Engineering

71

P RESSURE C ONVERSIONS PRESSURE CONVERSIONS To convert PSI to Feet of Water, find PSI value in the middle column and read Feet of Water in right hand column. To convert Feet of Water to PSI, find Feet of Water value in the middle column and read PSI in left hand column.

72

1 2 3 4

Feet of Water Head 2.31 4.62 6.93 9.24

PSI 28.14 28.57 29.00 29.44

65 66 67 68

Feet of Water Head 150.15 152.46 154.77 157.08

PSI 55.84 56.28 56.71 57.14

Feet of Water Head 129 297.99 130 300.30 131 302.61 132 304.92

PSI 83.55 83.98 84.42 84.85

Feet of Water Head 193 445.83 194 448.14 195 450.45 196 452.76

PSI 111.26 111.69 112.12 112.55

Feet of Water Head 257 593.67 258 595.98 259 598.29 260 600.60

2.16 2.60 3.03 3.46

5 6 7 8

11.55 13.86 16.17 18.48

29.87 30.30 30.74 31.17

69 70 71 72

159.39 161.70 164.01 166.32

57.58 58.01 58.44 58.87

133 134 135 136

307.23 309.54 311.85 314.16

85.28 85.71 86.15 86.58

197 198 199 200

455.07 457.38 459.69 462.00

112.99 113.42 113.85 114.29

261 262 263 264

602.91 605.22 607.53 609.84

3.90 4.33 4.76 5.19

9 10 11 12

20.79 23.10 25.41 27.72

31.60 32.03 32.47 32.90

73 74 75 76

168.63 170.94 173.25 175.56

59.31 59.74 60.17 60.61

137 138 139 140

316.47 318.78 321.09 323.40

87.01 87.45 87.88 88.31

201 202 203 204

464.31 466.62 468.93 471.24

114.72 116.88 119.05 121.21

265 270 275 280

612.15 623.70 635.25 646.80

5.63 6.06 6.49 6.93

13 14 15 16

30.03 32.34 34.65 36.96

33.33 33.77 34.20 34.63

77 78 79 80

177.87 180.18 182.49 184.80

61.04 61.47 61.90 62.34

141 142 143 144

325.71 328.02 330.33 332.64

88.74 89.18 89.61 90.04

205 206 207 208

473.55 475.86 478.17 480.48

123.38 125.54 127.71 129.87

285 290 295 300

658.35 669.90 681.45 693.00

7.36 7.79 8.23 8.66

17 18 19 20

39.27 41.58 43.89 46.20

35.06 35.50 35.93 36.36

81 82 83 84

187.11 189.42 191.73 194.04

62.77 63.20 63.64 64.07

145 146 147 148

334.95 337.26 339.57 341.88

90.48 90.91 91.34 91.77

209 210 211 212

482.79 485.10 487.41 489.72

132.03 134.20 136.36 138.53

305 310 315 320

704.55 716.10 727.65 739.20

9.09 9.52 9.96 10.39

21 22 23 24

48.51 50.82 53.13 55.44

36.80 37.23 37.66 38.10

85 86 87 88

196.35 198.66 200.97 203.28

64.50 64.94 65.37 65.80

149 150 151 152

344.19 346.50 348.81 351.12

92.21 92.64 93.07 93.51

213 214 215 216

492.03 494.34 496.65 498.96

140.69 142.86 145.02 147.19

325 330 335 340

750.75 762.30 773.85 785.40

10.82 11.26 11.69 12.12

25 26 27 28

57.75 60.06 62.37 64.68

38.53 38.96 39.39 39.83

89 90 91 92

205.59 207.90 210.21 212.52

66.23 66.67 67.10 67.53

153 154 155 156

353.43 355.74 358.05 360.36

93.94 94.37 94.81 95.24

217 218 219 220

501.27 503.58 505.89 508.20

149.35 151.52 153.68 155.84

345 350 355 360

796.95 808.50 820.05 831.60

12.55 12.99 13.42 13.85

29 30 31 32

66.99 69.30 71.61 73.92

40.26 40.69 41.13 41.56

93 94 95 96

214.83 217.14 219.45 221.76

67.97 68.40 68.83 69.26

157 158 159 160

362.67 364.98 367.29 369.60

95.67 96.10 96.54 96.97

221 222 223 224

510.51 512.82 515.13 517.44

158.01 160.17 162.34 164.50

365 370 375 380

843.15 854.70 866.25 877.80

14.29 14.72 15.15 15.58

33 34 35 36

76.23 78.54 80.85 83.16

41.99 42.42 42.86 43.29

97 98 99 100

224.07 226.38 228.69 231.00

69.70 70.13 70.56 71.00

161 162 163 164

371.91 374.22 376.53 378.84

97.40 97.84 98.27 98.70

225 226 227 228

519.75 522.06 524.37 526.68

166.67 168.83 171.00 173.16

385 390 395 400

889.35 900.90 912.45 924.00

16.02 16.45 16.88 17.32

37 38 39 40

85.47 87.78 90.09 92.40

43.72 44.16 44.59 45.02

101 102 103 104

233.31 235.62 237.93 240.24

71.43 71.86 72.29 72.73

165 166 167 168

381.15 383.46 385.77 388.08

99.13 99.57 100.00 100.43

229 230 231 232

528.99 531.30 533.61 535.92

183.98 194.81 205.63 216.45

425 450 475 500

981.75 1,040 1,097 1,155

17.75 18.18 18.61 19.05

41 42 43 44

94.71 97.02 99.33 101.64

45.45 45.89 46.32 46.75

105 106 107 108

242.55 244.86 247.17 249.48

73.16 73.59 74.03 74.46

169 170 171 172

390.39 392.70 395.01 397.32

100.87 101.30 101.73 102.16

233 234 235 236

538.23 540.54 542.85 545.16

227.27 238.10 248.92 259.74

525 550 575 600

1,213 1,271 1,328 1,386

19.48 19.91 20.35 20.78

45 46 47 48

103.95 106.26 108.57 110.88

47.19 47.62 48.05 48.48

109 110 111 112

251.79 254.10 256.41 258.72

74.89 75.32 75.76 76.19

173 174 175 176

399.63 401.94 404.25 406.56

102.60 103.03 103.46 103.90

237 238 239 240

547.47 549.78 552.09 554.40

270.56 281.39 292.21 303.03

625 650 675 700

1,444 1,502 1,559 1,617

21.21 21.65 22.08 22.51

49 50 51 52

113.19 115.50 117.81 120.12

48.92 49.35 49.78 50.22

113 114 115 116

261.03 263.34 265.65 267.96

76.62 77.06 77.49 77.92

177 178 179 180

408.87 411.18 413.49 415.80

104.33 104.76 105.19 105.63

241 242 243 244

556.71 559.02 561.33 563.64

313.85 324.68 335.50 346.32

725 750 775 800

1,675 1,733 1,790 1,848

22.94 23.38 23.81 24.24

53 54 55 56

122.43 124.74 127.05 129.36

50.65 51.08 51.52 51.95

117 118 119 120

270.27 272.58 274.89 277.20

78.35 78.79 79.22 79.65

181 182 183 184

418.11 420.42 422.73 425.04

106.06 106.49 106.93 107.36

245 246 247 248

565.95 568.26 570.57 572.88

357.14 367.97 378.79 389.61

825 850 875 900

1,906 1,964 2,021 2,079

24.68 25.11 25.54 25.97

57 58 59 60

131.67 133.98 136.29 138.60

52.38 52.81 53.25 53.68

121 122 123 124

279.51 281.82 284.13 286.44

80.09 80.52 80.95 81.39

185 186 187 188

427.35 429.66 431.97 434.28

107.79 108.23 108.66 109.09

249 250 251 252

575.19 577.50 579.81 582.12

400.43 411.26 422.08 432.90

925 950 975 1000

2,137 2,195 2,252 2,310

26.41 26.84 27.27 27.71

61 62 63 64

140.91 143.22 145.53 147.84

54.11 54.55 54.98 55.41

125 126 127 128

288.75 291.06 293.37 295.68

81.82 82.25 82.68 83.12

189 190 191 192

436.59 438.90 441.21 443.52

109.52 109.96 110.39 110.82

253 254 255 256

584.43 586.74 589.05 591.36

649.4 865.8 1,082 1,300

1500 2000 2500 3000

3,465 4,620 5,780 6,930

PSI 0.43 0.87 1.30 1.73

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P ROPERTIES

OF

W ATER , F RACTIONAL C ONVERSIONS

PROPERTIES OF WATER AT SATURATION PRESSURE Saturation Density Convert Factor Absolute Temp Pressure Density Density ft. of water Viscosity °F PSI (abs) lb/ft3 lb/gal to PSI lb/sec. ft. 32 0.0885 62.42 8.346 2.307 0.001203 40 0.1217 62.43 8.347 2.307 0.001042 50 0.1781 62.41 8.344 2.307 0.000880 60 0.2563 62.37 8.339 2.309 0.000753 70 80 90 100

0.3631 0.5069 0.6982 0.9492

62.30 62.22 62.12 62.00

8.330 8.319 8.305 8.289

2.311 2.315 2.318 2.323

0.000657 0.000579 0.000513 0.000460

110 120 130 140

1.275 1.692 2.222 2.889

61.84 61.73 61.54 61.39

8.268 8.253 8.228 8.208

2.328 2.333 2.340 2.346

0.000415 0.000376 0.000343 0.000316

150 160 170 180

3.718 4.741 5.992 7.510

61.20 61.01 60.79 60.57

8.182 8.157 8.128 8.098

2.353 2.360 2.369 2.377

0.000290 0.000269 0.000250 0.000233

190 200 210 212

9.339 11.53 14.12 14.696

60.35 60.13 59.88 59.81

8.069 8.039 8.006 7.997

2.386 2.395 2.405 2.408

0.000218 0.000205 0.000193 0.000191

220 230 240 250

17.19 20.78 24.97 29.82

59.63 59.38 59.10 58.82

7.973 7.939 7.902 7.864

2.415 2.425 2.436 2.448

0.000181 0.000171 0.000163 0.000154

275 300 350 400

45.42 67.01 134.6 247.3

58.09 57.31 55.59 53.65

7.767 7.662 7.432 7.173

2.479 2.513 2.591 2.684

0.000136 0.000124 0.000108 0.0000874

450 500 550 600

422.6 680.8 1045 1543

51.55 49.02 45.87 42.37

6.892 6.554 6.133 5.665

2.793 2.938 3.139 3.399

0.0000806 0.0000672 0.0000605 0.0000538

650 700

2208 3094

37.31 27.10

4.988 3.623

3.860 5.314

0.0000470 0.0000269

Decimal Equiv. –––––––––––– Fraction 0.015625 –– 1⁄64 0.031250 ––––– 1⁄32 0.046875 –– 3⁄64 0.062500 –––––––– 1⁄16 0.078125 –– 5⁄64 0.093750 ––––– 3⁄32 0.109375 –– 7⁄64 0.125000 –––––––––––– 1⁄8 0.140625 –– 9⁄64 0.156250 ––––– 5⁄32 0.171875 –– 11⁄64 0.187500 –––––––– 3⁄16 0.203125 –– 13⁄64 0.218750 ––––– 7⁄32 0.234375 –– 15⁄64 0.250000 ––––––––––––––– 1⁄4

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Decimal Foot –– Inch Measurement

Decimal Foot ––– Inch Measurement

Decimal –––– Inch Foot ––– Measurement

0.001302 0.002604 0.003906 0.005208 0.006510 0.007813 0.009115 0.010417 0.011719 0.013021 0.014323 0.015625 0.016927 0.018229 0.019531 0.020833 0.022135 0.023438 0.024740 0.026042 0.027344 0.028646 0.029948 0.031250 0.032552 0.033854 0.035156 0.036458 0.037760 0.039063 0.040365 0.041667

0.042969 0.044271 0.045573 0.046875 0.048177 0.049479 0.050781 0.052083 0.053385 0.054688 0.055990 0.057292 0.058594 0.059896 0.061198 0.062500 0.063802 0.065104 0.066406 0.067708 0.069010 0.070313 0.071615 0.072917 0.074219 0.075521 0.076823 0.078125 0.079427 0.080729 0.082031 0.083333

0.166667 0.250000 0.333333 0.416667 0.500000 0.583333 0.666667 0.750000 0.833333 0.916667 1.000000

– 1/64" ––– 1/32" – 3/64" ––––– 1/16" – 5/64" ––– 3/32" – 7/64" –––––––– 1/8" – 9/64" ––– 5/32" 11/64" ––––– 3/16" 13/64" ––– 7/32" 15/64" –––––––––– 1/4" 17/64" ––– 9/32" 19/64" ––––– 5/16" 21/64" ––– 11/32" 23/64" –––––––– 3/8" 25/64" ––– 13/32" 27/64" ––––– 7/16" 29/64" ––– 15/32" 31/64" –––––––––––– 1/2"

Decimal Equiv. –––––––––––– Fraction 0.265625 –– 17⁄64 0.281250 ––––– 9⁄32 0.296875 –– 19⁄64 0.312500 –––––––– 5⁄16 0.328125 –– 21⁄64 0.343750 ––––– 11⁄32 0.359375 –– 23⁄64 0.375000 –––––––––––– 3⁄8 0.390625 –– 25⁄64 0.406250 ––––– 13⁄32 0.421875 –– 27⁄64 0.437500 –––––––– 7⁄16 0.453125 –– 29⁄64 0.468750 ––––– 15⁄32 0.484375 –– 31⁄64 0.500000 –––––––––––––––––– 1⁄2

33/64" ––– 17/32" 35/64" ––––– 9/16" 37/64" ––– 19/32" 39/64" –––––––– 5/8" 41/64" ––– 21/32" 43/64" ––––– 11/16" 45/64" ––– 23/32" 47/64" –––––––––– 3/4" 49/64" ––– 25/32" 51/64" ––––– 13/16" 53/64" ––– 27/32" 55/64" –––––––– 7/8" 57/64" ––– 29/32" 59/64" ––––– 15/16" 61/64" ––– 31/32" 63/64" ––––––––––––– 1"

Decimal Equiv. –––––––––––– Fraction 0.515625 –– 33⁄64 0.531250 ––––– 17⁄32 0.546875 –– 35⁄64 0.562500 –––––––– 9⁄16 0.578125 –– 37⁄64 0.593750 ––––– 19⁄32 0.609375 –– 39⁄64 0.625000 –––––––––––– 5⁄8 0.640625 –– 41⁄64 0.656250 ––––– 21⁄32 0.671875 –– 43⁄64 0.687500 –––––––– 11⁄16 0.703125 –– 45⁄64 0.718750 ––––– 23⁄32 0.734375 –– 47⁄64 0.750000 ––––––––––––––– 3⁄4

–––––––––– 2" –––––––––– 3" –––––––––– 4" –––––––––– 5" –––––––––– 6" –––––––––– 7" –––––––––– 8" –––––––––– 9" –––––––––– 10" –––––––––– 11" –––––––––– 12"

Decimal Equiv. –––––––––––– Fraction 0.765625 –– 49⁄64 0.781250 ––––– 25⁄32 0.796875 –– 51⁄64 0.812500 –––––––– 13⁄16 0.828125 –– 53⁄64 0.843750 ––––– 27⁄32 0.859375 –– 55⁄64 0.875000 –––––––––––– 7⁄8 0.890625 –– 57⁄64 0.906250 ––––– 29⁄32 0.921875 –– 59⁄64 0.937500 –––––––– 15⁄16 0.953125 –– 61⁄64 0.968750 ––––– 31⁄32 0.984375 –– 63⁄64 1.000000 –––––––––––––––––– 1

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73

M ETRIC C ONVERSIONS

Inch 0 1 ⁄128 1 ⁄64 3 ⁄128 1 ⁄32 5 ⁄128 3 ⁄64 7 ⁄128 1 ⁄16 1

⁄16 1 ⁄8 3 ⁄16 1 ⁄4 5 ⁄16 3 ⁄8 7 ⁄16 1 ⁄2 9 ⁄16 5 ⁄8 11 ⁄16 3 ⁄4 13 ⁄16 7 ⁄8 15 ⁄16 1 11⁄16 11⁄8 13⁄16 11⁄4 15⁄16 13⁄8 17⁄16 11⁄2 19⁄16 15⁄8 111⁄16 13⁄4 113⁄16 17⁄8 115⁄16 2 Feet 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20

74

Millimeters 0 0.1984375 0.396875 0.5953125 0.79375 0.9921875 1.190625 1.3890625 1.5875 1.5875 3.175 4.7625 6.35 7.9375 9.525 11.1125 12.7 14.2875 15.875 17.4625 19.05 20.6375 22.225 23.8125 25.4 26.9875 28.575 30.1625 31.75 33.3375 34.925 36.5125 38.1 39.6875 41.275 42.8625 44.45 46.0375 47.625 49.2125 50.8 Meters 0.3048 0.6096 0.9144 1.2192 1.524 1.8288 2.1336 2.4384 2.7432 3.048 3.3528 3.6576 3.9624 4.2672 4.572 4.8768 5.1816 5.4864 5.7912 6.096

METRIC CONVERSION TABLE Example: Convert 3.7664 meters to feet, inches and fractions Using the feet to meter table, 12 ft. = 3.6576 So now convert 3.7664m - 3.6576m = 108.8mm Using the inch to millimeter table, 41⁄4 in. = 107.95mm So now convert 108.8mm - 107.95mm = 0.85mm Using the inch to millimeter table, 1⁄32 = 0.79375

Example: Convert 15 ft. 67⁄16 in. to meters Using the feet to meter table, 15 ft. = 4.572 meters Using the inch to millimeter table, 67⁄16 in. = .1635125 meters Thus, 15 ft. 67⁄16 in. = 4.7355125 meters

Inch Millimeters 21⁄16 52.3875 21⁄8 53.975 23⁄16 55.5625 21⁄4 57.15 25⁄16 58.7375 23⁄8 60.325 27⁄16 61.9125 21⁄2 63.5 29⁄16 65.0875 25⁄8 66.675 211⁄16 68.2625 23⁄4 69.85 213⁄16 71.4375 27⁄8 73.025 215⁄16 74.6125 3 76.2 31⁄16 77.7875 31⁄8 79.375 33⁄16 80.9625 31⁄4 82.55 35⁄16 84.1375 33⁄8 85.725 37⁄16 87.3125 31⁄2 88.9 39⁄16 90.4875 35⁄8 92.075 311⁄16 93.6625 33⁄4 95.25 313⁄16 96.8375 37⁄8 98.425 315⁄16 100.0125 4 101.6

Inch Millimeters 41⁄16 103.1875 41⁄8 104.775 43⁄16 106.3625 41⁄4 107.95 45⁄16 109.5375 43⁄8 111.125 47⁄16 112.7125 41⁄2 114.3 49⁄16 115.8875 45⁄8 117.475 411⁄16 119.0625 43⁄4 120.65 413⁄16 122.2375 47⁄8 123.825 415⁄16 125.4125 5 127 51⁄16 128.5875 51⁄8 130.175 53⁄16 131.7625 51⁄4 133.35 55⁄16 134.9375 53⁄8 136.525 57⁄16 138.1125 51⁄2 139.7 59⁄16 141.2875 55⁄8 142.875 511⁄16 144.4625 53⁄4 146.05 513⁄16 147.6375 57⁄8 149.225 515⁄16 150.8125 6 152.4

InchMillimeters 61⁄16 153.9875 61⁄8 155.575 63⁄16 157.1625 61⁄4 158.75 65⁄16 160.3375 63⁄8 161.925 67⁄16 163.5125 61⁄2 165.1 69⁄16 166.6875 65⁄8 168.275 611⁄16 169.8625 63⁄4 171.45 613⁄16 173.0375 67⁄8 174.625 615⁄16 176.2125 7 177.8 71⁄16 179.3875 71⁄8 180.975 73⁄16 182.5625 71⁄4 184.15 75⁄16 185.7375 73⁄8 187.325 77⁄16 188.9125 71⁄2 190.5 79⁄16 192.0875 75⁄8 193.675 711⁄16 195.2625 73⁄4 196.85 713⁄16 198.4375 77⁄8 200.025 715⁄16 201.6125 8 203.2

InchMillimeters 81⁄16 204.7875 81⁄8 206.375 83⁄16 207.9625 81⁄4 209.55 85⁄16 211.1375 83⁄8 212.725 87⁄16 214.3125 81⁄2 215.9 89⁄16 217.4875 85⁄8 219.075 811⁄16 220.6625 83⁄4 222.25 813⁄16 223.8375 87⁄8 225.425 815⁄16 227.0125 9 228.6 91⁄16 230.1875 91⁄8 231.775 93⁄16 233.3625 91⁄4 234.95 95⁄16 236.5375 93⁄8 238.125 97⁄16 239.7125 91⁄2 241.3 99⁄16 242.8875 95⁄8 244.475 911⁄16 246.0625 93⁄4 247.65 913⁄16 249.2375 97⁄8 250.825 915⁄16 252.4125 10 254

Feet 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40

Feet 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Feet 61 62 63 64 65 66 67 68 69 70 71 72 73 74 75 76 77 78 79 80

Feet 81 82 83 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98 99 100

Meters 6.4008 6.7056 7.0104 7.3152 7.62 7.9248 8.2296 8.5344 8.8392 9.144 9.4488 9.7536 10.0584 10.3632 10.668 10.9728 11.2776 11.5824 11.8872 12.192

Meters 12.4968 12.8016 13.1064 13.4112 13.716 14.0208 14.3256 14.6304 14.9352 15.24 15.5448 15.8496 16.1544 16.4592 16.764 17.0688 17.3736 17.6784 17.9832 18.288

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Meters 18.5928 18.8976 19.2024 19.5072 19.812 20.1168 20.4216 20.7264 21.0312 21.336 21.6408 21.9456 22.2504 22.5552 22.86 23.1648 23.4696 23.7744 24.0792 24.384

InchMillimeters 101⁄16 255.5875 101⁄8 257.175 103⁄16 258.7625 101⁄4 260.35 105⁄16 261.9375 103⁄8 263.525 107⁄16 265.1125 101⁄2 266.7 109⁄16 268.2875 105⁄8 269.875 1011⁄16 271.4625 103⁄4 273.05 1013⁄16 274.6375 107⁄8 276.225 1015⁄16 277.8125 11 279.4 111⁄16 280.9875 111⁄8 282.575 113⁄16 284.1625 111⁄4 285.75 115⁄16 287.3375 113⁄8 288.925 117⁄16 290.5125 111⁄2 292.1 119⁄16 293.6875 115⁄8 295.275 1111⁄16 296.8625 113⁄4 298.45 1113⁄16 300.0375 117⁄8 301.625 1115⁄16 303.2125 12 304.8

Meters 24.6888 24.9936 25.2984 25.6032 25.908 26.2128 26.5176 26.8224 27.1272 27.432 27.7368 28.0416 28.3464 28.6512 28.956 29.2608 29.5656 29.8704 30.1752 30.48

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P ROPERTIES

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P IPE Note: † The ferritic steels may be about 5% less, and the austenitic stainless steels about 2% greater than the values shown in this table which are based on weights for carbon steel. * Schedule Numbers Standard weight pipe and schedule 40 are the same in all sizes through l0-inch from 12-inch through 24-inch, standard weight pipe has a wall thickness of 3/8-inch. Extra strong weight pipe and schedule 80 are the same in all sizes through 8-inch; from 8-inch through 24-inch, extra strong weight pipe has a wall thickness of 1⁄2". Double extra strong weight pipe has no corresponding schedule number. a: ANSI B36.10 steel pipe schedule numbers b: ANSI B36.10 steel pipe nominal wall thickness designation c: ANSI B36.19 stainless steel pipe schedule numbers

The following formulas are used in the computation of the values shown in the table: †weight of pipe per foot (pounds) = 10.6802t (D - t) weight of water per foot (pounds) = 0.3405 x d 2 square feet outside surface per foot = π/12 x D squarefeet inside surface perfoot = π/12 x d inside area (square inches) = π/4 x d 2 area of metal (square inches) = π/4 x (D2 - d 2 ) 2 moment of inertia (inches4) = π/64 x (D2 - d 2 ) = AmR g section modulus (inches3) = π/32 x (D4 - d 4 )/D radius of gyration (inches) = Where: Am d D Rg t

(D2 - d 2)/4

= area of metal (square inches) = inside diameter (inches) = outside diameter (inches) = radius of gyration (inches) = pipewall thickness(inches)

Nom. Pipe Size, O.D. Inches 1

Schedule Number* a b c

0.0740 0.0568 0.0363 0.132 0.104 0.072 0.233 0.191 0.141 0.396 0.357 0.304 0.234 0.171 0.050 0.665 0.614 0.533 0.432 0.296 0.148 1.103 0.945

0.0548 0.0720 0.0925 0.0970 0.125 0.157 0.125 0.167 0.217 0.158 0.197 0.250 0.320 0.384 0.504 0.201 0.252 0.333 0.433 0.570 0.718 0.255 0.413

Weight Outside Inside Weight of Water Surface Surface per Foot per Foot Sq. Ft./Ft. Sq. Ft./Ft. Lbs.† Lbs.

1

40

Std 40S

0.133

1.049

0.864

0.494

0.344

0.2746

1.68

0.375

1.3150

80 160 – – – 40 80 160 –

XS – XXS – – Std XS – XXS

0.179 0.250 0.358 0.065 0.109 0.140 0.191 0.250 0.382

0.957 0.815 0.599 1.530 1.442 1.380 1.278 1.160 0.896

0.719 0.522 0.282 1.839 1.633 1.496 1.283 1.057 0.631

0.639 0.836 1.076 0.326 0.531 0.669 0.881 1.107 1.534

0.344 0.344 0.344 0.435 0.435 0.435 0.435 0.435 0.435

0.2505 0.2134 0.1568 0.4006 0.3775 0.3613 0.3346 0.3037 0.2346

2.17 2.84 3.66 1.11 1.81 2.27 3.00 3.76 5.21

0.312 0.226 0.122 0.797 0.708 0.648 0.556 0.458 0.273

1

⁄4

3

⁄8

0.6750

1

⁄2

0.8400

3

⁄4

1.0500

11⁄4 1.6600

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80S – – 5S 10S 40S 80S – –

0.307 0.269 0.215 0.410 0.364 0.302 0.545 0.493 0.423 0.710 0.674 0.622 0.546 0.466 0.252 0.920 0.884 0.824 0.742 0.614 0.434 1.185 1.097

Metal Area Sq. In.

– Std XS – Std XS – Std XS – – Std XS – XXS – – Std XS – XXS – –

0.5400

0.049 0.068 0.095 0.065 0.088 0.119 0.065 0.091 0.126 0.065 0.083 0.109 0.147 0.187 0.294 0.065 0.083 0.113 0.154 0.218 0.308 0.065 0.109

Inside Area Sq. In.

– 40 80 – 40 80 – 40 80 – – 40 80 160 – – – 40 80 160 – – –

⁄8

0.4050

10S 40S 80S 10S 40S 80S 10S 40S 80S 5S 10S 40S 80S – – 5S 10S 40S 80S – – 5S 10S

Wall Inside Thickness Diameter Inch Inch

0.106 0.106 0.106 0.141 0.141 0.141 0.177 0.177 0.177 0.220 0.220 0.220 0.220 0.220 0.220 0.275 0.275 0.275 0.275 0.275 0.275 0.344 0.344

0.0804 0.0704 0.0563 0.1073 0.0953 0.0791 0.1427 0.1291 0.1107 0.1859 0.1765 0.1628 0.1429 0.1220 0.0660 0.2409 0.2314 0.2157 0.1943 0.1607 0.1136 0.3102 0.2872

0.186 0.245 0.315 0.330 0.425 0.535 0.423 0.568 0.739 0.538 0.671 0.851 1.09 1.30 1.71 0.684 0.857 1.13 1.47 1.94 2.44 0.868 1.40

0.0321 0.0246 0.0157 0.0572 0.0451 0.0311 0.1011 0.0828 0.0609 0.172 0.155 0.132 0.102 0.074 0.022 0.288 0.266 0.231 0.187 0.128 0.064 0.478 0.410

Moment Section of Inertia Modulus In.4 In.3 0.00088 0.00106 0.00122 0.00279 0.00331 0.00377 0.00586 0.00729 0.00862 0.01197 0.01431 0.01709 0.02008 0.02212 0.02424 0.02450 0.02969 0.03704 0.04479 0.05269 0.05792 0.04999 0.07569

Radius Gyration In.

0.00437 0.00525 0.00600 0.0103 0.0123 0.0139 0.0174 0.0216 0.0255 0.0285 0.0341 0.0407 0.0478 0.0527 0.0577 0.0467 0.0566 0.0705 0.0853 0.1004 0.1103 0.0760 0.1151

0.1271 0.1215 0.1146 0.1695 0.1628 0.1547 0.2169 0.2090 0.1991 0.2750 0.2692 0.2613 0.2505 0.2402 0.2192 0.349 0.343 0.334 0.321 0.304 0.284 0.443 0.428

0.08734

0.1328

0.421

0.10561 0.12512 0.14046 0.10375 0.16049 0.19471 0.24179 0.28386 0.34110

0.1606 0.1903 0.2136 0.1250 0.1934 0.2346 0.2913 0.3420 0.4110

0.407 0.387 0.361 0.564 0.550 0.540 0.524 0.506 0.472

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75

P ROPERTIES Nom. Pipe Size, O.D. Inches

Schedule Number* a b c

Inside Area Sq. In.

Metal Area Sq. In.

Weight Outside Inside Weight of Water Surface Surface per Foot per Foot Sq. Ft./Ft. Sq. Ft./Ft. Lbs.† Lbs.

Moment Section of Inertia Modulus In.4 In.3

P IPE

Radius Gyration In.

–

–

5S

0.065

1.770

2.461

0.375

0.497

0.4634

1.27

1.067

0.15792

0.1662

0.649

–

–

10S

0.109

1.682

2.222

0.613

0.497

0.4403

2.08

0.963

0.24682

0.2598

0.634

40

Std 40S

0.145

1.610

2.036

0.799

0.497

0.4215

2.72

0.883

0.30989

0.3262

0.623

11⁄2

80

XS 80S

0.200

1.500

1.767

1.068

0.497

0.3927

3.63

0.766

0.39121

0.4118

0.605

1.9000

160

–

–

0.281

1.338

1.406

1.429

0.497

0.3503

4.86

0.610

0.48239

0.5078

0.581

–

XXS

–

0.400

1.100

0.950

1.885

0.497

0.2880

6.41

0.412

0.56784

0.5977

0.549

–

–

–

0.525

0.850

0.567

2.268

0.497

0.2225

7.71

0.246

0.61409

0.6464

0.520

–

–

–

0.650

0.600

0.283

2.553

0.497

0.1571

8.68

0.123

0.63335

0.6667

0.498

–

–

5S

0.065

2.245

3.958

0.472

0.622

0.5877

1.60

1.716

0.31489

0.2652

0.817

–

–

10S

0.109

2.157

3.654

0.776

0.622

0.5647

2.64

1.584

0.49919

0.4204

0.802

40

Std 40S

0.154

2.067

3.356

1.075

0.622

0.5411

3.65

1.455

0.66575

0.5606

0.787

2

80

XS 80S

0.218

1.939

2.953

1.477

0.622

0.5076

5.02

1.280

0.86792

0.7309

0.766

2.3750

160

–

–

0.343

1.689

2.241

2.190

0.622

0.4422

7.44

0.971

1.16232

0.9788

0.729

–

XXS

–

0.436

1.503

1.774

2.656

0.622

0.3935

9.03

0.769

1.31130

1.104

0.703

–

–

–

0.562

1.251

1.229

3.201

0.622

0.3275

10.9

0.533

1.44157

1.214

0.671

–

–

–

0.687

1.001

0.787

3.643

0.622

0.2621

12.4

0.341

1.51251

1.274

0.644

–

–

5S

0.083

2.709

5.764

0.728

0.753

0.7092

2.47

2.499

0.71002

0.4939

0.988

–

–

10S

0.120

2.635

5.453

1.039

0.753

0.6898

3.53

2.364

0.98725

0.6868

0.975

40

Std 40S

0.203

2.469

4.788

1.704

0.753

0.6464

5.79

2.076

1.52955

1.064

0.947

21⁄2

80

XS 80S

0.276

2.323

4.238

2.254

0.753

0.6082

7.66

1.837

1.92423

1.339

0.924

2.8750

160

–

–

0.375

2.125

3.547

2.945

0.753

0.5563

10.0

1.538

2.35274

1.637

0.894

–

XXS

–

0.552

1.771

2.463

4.028

0.753

0.4636

13.7

1.068

2.87079

1.997

0.844

–

–

–

0.675

1.525

1.827

4.665

0.753

0.3992

15.9

0.792

3.08819

2.148

0.814

–

–

–

0.800

1.275

1.277

5.215

0.753

0.3338

17.7

0.554

3.22396

2.243

0.786

–

–

5S

0.083

3.334

8.730

0.891

0.916

0.8728

3.03

3.785

1.30116

0.7435

1.208

–

–

76

Wall Inside Thickness Diameter Inch Inch

OF

10S

0.120

3.260

8.347

1.274

0.916

0.8535

4.33

3.619

1.82196

1.041

1.196

40

Std 40S

0.216

3.068

7.393

2.228

0.916

0.8032

7.58

3.205

3.01716

1.724

1.164

3

80

XS 80S

0.300

2.900

6.605

3.016

0.916

0.7592

10.3

2.864

3.89432

2.225

1.136

3.5000

160

–

–

0.437

2.626

5.416

4.205

0.916

0.6875

14.3

2.348

5.03192

2.875

1.094

–

XXS

–

0.600

2.300

4.155

5.466

0.916

0.6021

18.6

1.801

5.99251

3.424

1.047

–

–

–

0.725

2.050

3.301

6.320

0.916

0.5367

21.5

1.431

6.49924

3.714

1.014

–

–

–

0.850

1.800

2.545

7.076

0.916

0.4712

24.1

1.103

6.85088

3.915

0.984

–

–

5S

0.083

3.834

11.545

1.021

1.05

1.004

3.47

5.005

1.95972

0.9799

1.385

–

31⁄2

–

4.0000

40

10S

0.120

3.760

11.104

1.463

1.05

0.9844

4.97

4.814

2.75519

1.378

1.372

Std 40S

0.226

3.548

9.887

2.680

1.05

0.9289

9.11

4.286

4.78772

2.394

1.337

80

XS 80S

0.318

3.364

8.888

3.678

1.05

0.8807

12.5

3.853

6.28009

3.140

1.307

–

XXS

–

0.636

2.728

5.845

6.721

1.05

0.7142

22.9

2.534

9.84776

4.924

1.210

–

–

5S

0.083

4.334

14.753

1.152

1.18

1.135

3.92

6.396

2.80979

1.249

1.562

–

–

10S

0.120

4.260

14.253

1.651

1.18

1.115

5.61

6.179

3.96268

1.761

1.549

–

–

–

0.188

4.124

13.358

2.547

1.18

1.080

8.66

5.791

5.93033

2.636

1.526

40

Std 40S

0.237

4.026

12.730

3.174

1.18

1.054

10.8

5.519

7.23260

3.214

1.510

4

80

XS 80S

0.337

3.826

11.497

4.407

1.18

1.002

15.0

4.984

9.61049

4.271

1.477

4.5000

120

–

–

0.437

3.626

10.326

5.578

1.18

0.9493

19.0

4.477

11.6433

5.175

1.445

–

–

–

0.500

3.500

9.621

6.283

1.18

0.9163

21.4

4.171

12.7627

5.672

1.425

160

–

–

0.531

3.438

9.283

6.621

1.18

0.9001

22.5

4.025

13.2710

5.898

1.416

–

XXS

–

0.674

3.152

7.803

8.101

1.18

0.8252

27.5

3.383

15.2837

6.793

1.374

–

–

–

0.800

2.900

6.605

9.299

1.18

0.7592

31.6

2.864

16.6570

7.403

1.338

–

–

–

0.925

2.650

5.515

10.389

1.18

0.6938

35.3

2.391

17.7081

7.870

1.306

Anvil International, Piping & Pipe Hanger Design and Engineering

www.anvilintl.com

P ROPERTIES

Nom. Pipe Size, O.D. Inches

OF

P IPE

Schedule Number* a b c

Wall Inside Thickness Diameter Inch Inch

Inside Area Sq. In.

Metal Area Sq. In.

Weight Outside Inside Weight of Water Surface Surface per Foot per Foot Sq. Ft./Ft. Sq. Ft./Ft. Lbs.† Lbs.

Moment Section of Inertia Modulus In.4 In.3

Radius Gyration In.

–

–

5S

0.109

5.345

22.438

1.868

1.46

1.399

6.35

9.728

6.94713

2.498

1.929

–

–

10S

0.134

5.295

22.020

2.285

1.46

1.386

7.77

9.547

8.42536

3.029

1.920

40

Std 40S

0.258

5.047

20.006

4.300

1.46

1.321

14.6

8.673

15.1622

5.451

1.878

5

80

XS 80S

0.375

4.813

18.194

6.112

1.46

1.260

20.8

7.888

20.6707

7.431

1.839

5.5630

120

–

–

0.500

4.563

16.353

7.953

1.46

1.195

27.0

7.090

25.7317

9.251

1.799

160

–

–

0.625

4.313

14.610

9.696

1.46

1.129

33.0

6.334

30.0259

10.79

1.760

–

XXS

–

0.750

4.063

12.965

11.340

1.46

1.064

38.6

5.621

33.6348

12.09

1.722

–

–

–

0.875

3.813

11.419

12.887

1.46

0.9982

43.8

4.951

36.6355

13.17

1.686

–

–

–

1.000

3.563

9.971

14.335

1.46

0.9328

48.7

4.323

39.1007

14.06

1.652

–

–

5S

0.109

6.407

32.240

2.231

1.73

1.677

7.59

13.98

11.8454

3.576

2.304

–

–

10S

0.134

6.357

31.739

2.733

1.73

1.664

9.29

13.76

14.3974

4.346

2.295

–

–

–

0.129

6.367

31.839

2.633

1.73

1.667

8.95

13.80

13.8918

4.194

2.297

6 6.6250

40

Std 40S

0.280

6.065

28.890

5.581

1.73

1.588

19.0

12.53

28.1422

8.496

2.245

80

XS 80S

0.432

5.761

26.067

8.405

1.73

1.508

28.6

11.30

40.4907

12.22

2.195

120

–

–

0.562

5.501

23.767

10.705

1.73

1.440

36.4

10.30

49.6106

14.98

2.153

160

–

–

0.718

5.189

21.147

13.324

1.73

1.358

45.3

9.168

58.9732

17.80

2.104

–

XXS

–

0.864

4.897

18.834

15.637

1.73

1.282

53.2

8.165

66.3326

20.02

2.060

–

–

–

1.000

4.625

16.800

17.671

1.73

1.211

60.1

7.284

72.1009

21.77

2.020

–

–

–

1.125

4.375

15.033

19.439

1.73

1.145

66.1

6.517

76.5775

23.12

1.985

–

–

5S

0.109

8.407

55.510

2.916

2.26

2.201

9.91

24.07

26.4402

6.131

3.011

–

–

10S

0.148

8.329

54.485

3.941

2.26

2.181

13.4

23.62

35.4145

8.212

2.998

–

–

–

0.219

8.187

52.643

5.783

2.26

2.143

19.7

22.82

51.1172

11.85

2.973

20

–

–

0.250

8.125

51.849

6.578

2.26

2.127

22.4

22.48

57.7220

13.38

2.962

30

–

–

0.277

8.071

51.162

7.265

2.26

2.113

24.7

22.18

63.3527

14.69

2.953

40 8 8.6250

Std 40S

60 80

–

XS 80S

10.7500

0.322

7.981

50.027

8.399

2.26

2.089

28.6

21.69

72.4892

16.81

2.938

0.406

7.813

47.943

10.483

2.26

2.045

35.6

20.79

88.7363

20.58

2.909

0.500

7.625

45.664

12.763

2.26

1.996

43.4

19.80

105.716

24.51

2.878

100

–

–

0.593

7.439

43.463

14.963

2.26

1.948

50.9

18.84

121.324

28.13

2.847

120

–

–

0.718

7.189

40.591

17.836

2.26

1.882

60.6

17.60

140.535

32.59

2.807

140

–

–

0.812

7.001

38.496

19.931

2.26

1.833

67.8

16.69

153.722

35.65

2.777

160

–

–

0.906

6.813

36.456

21.970

2.26

1.784

74.7

15.80

165.887

38.47

2.748

–

–

–

1.000

6.625

34.472

23.955

2.26

1.734

81.4

14.94

177.087

41.06

2.719

–

–

–

1.125

6.375

31.919

26.507

2.26

1.669

90.1

13.84

190.572

44.19

2.681

–

–

5S

0.134

10.482

86.294

4.469

2.81

2.744

15.2

37.41

62.9675

11.71

3.75

–

–

10S

0.165

10.420

85.276

5.487

2.81

2.728

18.7

36.97

76.8638

14.30

3.74

–

–

–

0.219

10.312

83.517

7.245

2.81

2.700

24.6

36.21

100.485

18.69

3.72

20

–

–

0.250

10.250

82.516

8.247

2.81

2.683

28.0

35.77

113.714

21.16

3.71

–

–

3.69

30 10

–

0.307

10.136

80.691

10.072

2.81

2.654

34.2

34.98

137.420

25.57

40

Std 40S

0.365

10.020

78.854

11.908

2.81

2.623

40.5

34.19

160.734

29.90

3.67

60

XS 80S

0.500

9.750

74.662

16.101

2.81

2.553

54.7

32.37

211.950

39.43

3.63

80

–

–

0.593

9.564

71.840

18.922

2.81

2.504

64.3

31.15

244.844

45.55

3.60

100

–

–

0.718

9.314

68.134

22.629

2.81

2.438

76.9

29.54

286.132

53.23

3.56

120

–

–

0.843

9.064

64.525

26.237

2.81

2.373

89.2

27.97

324.225

60.32

3.52

–

–

–

0.875

9.000

63.617

27.145

2.81

2.356

92.3

27.58

333.485

62.04

3.51

140

–

–

1.000

8.750

60.132

30.631

2.81

2.291

104

26.07

367.806

68.43

3.47

160

–

–

1.125

8.500

56.745

34.018

2.81

2.225

116

24.60

399.308

74.29

3.43

–

–

–

1.250

8.250

53.456

37.306

2.81

2.160

127

23.18

428.149

79.66

3.39

–

–

–

1.500

7.750

47.173

43.590

2.81

2.029

148

20.45

478.464

89.02

3.31

www.anvilintl.com

Anvil International, Piping & Pipe Hanger Design and Engineering

77

P ROPERTIES

Nom. Pipe Size, O.D. Inches

Schedule Number* a b c –

Inside Area Sq. In.

Metal Area Sq. In.

Weight Outside Inside Weight of Water Surface Surface per Foot per Foot Sq. Ft./Ft. Sq. Ft./Ft. Lbs.† Lbs.

Moment Section of Inertia Modulus In.4 In.3

P IPE

Radius Gyration In.

–

5S

0.156

12.438

121.504

6.172

3.34

3.256

21.0

52.68

122.389

19.20

4.45

–

–

10S

0.180

12.390

120.568

7.108

3.34

3.244

24.2

52.27

140.419

22.03

4.44

20

–

–

0.250

12.250

117.859

9.817

3.34

3.207

33.4

51.10

191.824

30.09

4.42

30

–

–

0.330

12.090

114.800

12.876

3.34

3.165

43.8

49.77

248.453

38.97

4.39

– 40 –

78

Wall Inside Thickness Diameter Inch Inch

OF

Std 40S –

–

XS 80S

0.375

12.000

113.097

14.579

3.34

3.142

49.6

49.03

279.335

43.82

4.38

0.406

11.938

111.932

15.745

3.34

3.125

53.5

48.53

300.209

47.09

4.37

0.500

11.750

108.434

19.242

3.34

3.076

65.4

47.01

361.544

56.71

4.33

12

60

–

–

0.562

11.626

106.157

21.519

3.34

3.044

73.2

46.02

400.420

62.81

4.31

12.7500

80

–

–

0.687

11.376

101.641

26.035

3.34

2.978

88.5

44.07

475.104

74.53

4.27

–

–

–

0.750

11.250

99.402

28.274

3.34

2.945

96.1

43.09

510.926

80.15

4.25

100

–

–

0.843

11.064

96.142

31.534

3.34

2.897

107

41.68

561.650

88.10

4.22

–

–

–

0.875

11.000

95.033

32.643

3.34

2.880

111

41.20

578.523

90.75

4.21

120

–

–

1.000

10.750

90.763

36.914

3.34

2.814

125

39.35

641.664

100.7

4.17

140

–

–

1.125

10.500

86.590

41.086

3.34

2.749

140

37.54

700.551

109.9

4.13

–

–

–

1.250

10.250

82.516

45.160

3.34

2.683

154

35.77

755.378

118.5

4.09

160

–

–

1.312

10.126

80.531

47.145

3.34

2.651

160

34.91

781.126

122.5

4.07

–

–

5S

0.156

13.688

147.153

6.785

3.67

3.584

23.1

63.80

162.564

23.22

4.89

–

–

10S

0.188

13.624

145.780

8.158

3.67

3.567

27.7

63.20

194.566

27.80

4.88

–

–

–

0.210

13.580

144.840

9.098

3.67

3.555

30.9

62.79

216.308

30.90

4.88

–

–

–

0.219

13.562

144.457

9.481

3.67

3.551

32.2

62.63

225.142

32.16

4.87

10

–

–

0.250

13.500

143.139

10.799

3.67

3.534

36.7

62.06

255.300

36.47

4.86

–

–

–

0.281

13.438

141.827

12.111

3.67

3.518

41.2

61.49

285.047

40.72

4.85

20

–

–

0.312

13.376

140.521

13.417

3.67

3.502

45.6

60.92

314.384

44.91

4.84 4.83

–

–

–

0.344

13.312

139.180

14.758

3.67

3.485

50.2

60.34

344.242

49.18

14

30

Std

–

0.375

13.250

137.886

16.052

3.67

3.469

54.6

59.78

372.760

53.25

4.82

14.0000

40

–

–

0.437

13.126

135.318

18.620

3.67

3.436

63.3

58.67

428.607

61.23

4.80

–

–

–

0.469

13.062

134.001

19.937

3.67

3.420

67.8

58.09

456.819

65.26

4.79

–

XS

–

0.500

13.000

132.732

21.206

3.67

3.403

72.1

57.54

483.756

69.11

4.78

60

–

–

0.593

12.814

128.961

24.977

3.67

3.355

84.9

55.91

562.287

80.33

4.74

–

–

–

0.625

12.750

127.676

26.262

3.67

3.338

89.3

55.35

588.530

84.08

4.73

80

–

–

0.750

12.500

122.718

31.220

3.67

3.272

106

53.20

687.318

98.19

4.69

100

–

–

0.937

12.126

115.485

38.453

3.67

3.175

131

50.07

824.436

117.8

4.63

120

–

–

1.093

11.814

109.618

44.320

3.67

3.093

151

47.52

929.521

132.8

4.58

140

–

–

1.250

11.500

103.869

50.069

3.67

3.011

170

45.03

1027.20

146.7

4.53

160

–

–

1.406

11.188

98.309

55.629

3.67

2.929

189

42.62

1116.65

159.5

4.48

–

–

5S

0.165

15.670

192.854

8.208

4.19

4.102

27.9

83.61

257.303

32.16

5.60

–

–

10S

0.188

15.624

191.723

9.339

4.19

4.090

31.7

83.12

291.904

36.49

5.59

10

–

–

0.250

15.500

188.692

12.370

4.19

4.058

42.1

81.81

383.664

47.96

5.57

20

–

–

0.312

15.376

185.685

15.377

4.19

4.025

52.3

80.50

473.248

59.16

5.55

30

Std

–

0.375

15.250

182.654

18.408

4.19

3.992

62.6

79.19

562.084

70.26

5.53

16

40

–

–

0.500

15.000

176.715

24.347

4.19

3.927

82.8

76.61

731.942

91.49

5.48

16.0000

60

–

–

0.656

14.688

169.440

31.622

4.19

3.845

108

73.46

932.336

116.5

5.43

80

–

–

0.843

14.314

160.921

40.141

4.19

3.747

136

69.77

1156.29

144.5

5.37

100

–

–

1.031

13.938

152.578

48.484

4.19

3.649

165

66.15

1364.43

170.6

5.30

120

–

–

1.218

13.564

144.499

56.563

4.19

3.551

192

62.65

1555.41

194.4

5.24

140

–

–

1.437

13.126

135.318

65.744

4.19

3.436

224

58.67

1759.86

220.0

5.17

160

–

–

1.593

12.814

128.961

72.101

4.19

3.355

245

55.91

1893.54

236.7

5.12

Anvil International, Piping & Pipe Hanger Design and Engineering

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P ROPERTIES

Nom. Pipe Size, O.D. Inches

OF

P IPE

Schedule Number* a b c

Wall Inside Thickness Diameter Inch Inch

Inside Area Sq. In.

Metal Area Sq. In.

Weight Outside Inside Weight of Water Surface Surface per Foot per Foot Sq. Ft./Ft. Sq. Ft./Ft. Lbs.† Lbs.

Moment Section of Inertia Modulus In.4 In.3

Radius Gyration In.

–

–

5S

0.165

17.670

245.224

9.245

4.71

4.626

31.4

106.3

367.621

40.85

6.31

–

–

10S

0.188

17.624

243.949

10.520

4.71

4.614

35.8

105.8

417.258

46.36

6.30

–

–

–

0.250

17.500

240.528

13.941

4.71

4.581

47.4

104.3

549.138

61.02

6.28

20

–

–

0.312

17.376

237.132

17.337

4.71

4.549

58.9

102.8

678.244

75.36

6.25

–

Std

–

0.375

17.250

233.705

20.764

4.71

4.516

70.6

101.3

806.631

89.63

6.23

30

–

–

0.437

17.126

230.357

24.112

4.71

4.484

82.0

99.87

930.264

103.4

6.21

18

–

XS

–

0.500

17.000

226.980

27.489

4.71

4.451

93.5

98.40

1053.17

117.0

6.19

18.0000

40

–

–

0.562

16.876

223.681

30.788

4.71

4.418

105

96.97

1171.49

130.2

6.17

60

–

–

0.750

16.500

213.825

40.644

4.71

4.320

138

92.70

1514.64

168.3

6.10

80

–

–

0.937

16.126

204.241

50.228

4.71

4.222

171

88.55

1833.47

203.7

6.04

100

–

–

1.156

15.688

193.297

61.172

4.71

4.107

208

83.80

2179.69

242.2

5.97

120

–

–

1.375

15.250

182.654

71.815

4.71

3.992

244

79.19

2498.09

277.6

5.90

140

–

–

1.562

14.876

173.805

80.664

4.71

3.895

274

75.35

2749.11

305.5

5.84

160

–

–

1.781

14.438

163.721

90.748

4.71

3.780

309

70.98

3019.96

335.6

5.77

–

–

5S

0.188

19.624

302.458

11.701

5.24

5.138

39.8

131.1

574.172

57.42

7.00

–

–

10S

0.218

19.564

300.611

13.548

5.24

5.122

46.1

130.3

662.796

66.28

6.99

10

–

–

0.250

19.500

298.648

15.512

5.24

5.105

52.7

129.5

756.434

75.64

6.98

20

Std

–

0.375

19.250

291.039

23.120

5.24

5.040

78.6

126.2

1113.47

111.3

6.94

30

XS

–

0.500

19.000

283.529

30.631

5.24

4.974

104

122.9

1456.86

145.7

6.90

20

40

–

–

0.593

18.814

278.005

36.155

5.24

4.925

123

120.5

1703.71

170.4

6.86

20.0000

60

–

–

0.812

18.376

265.211

48.948

5.24

4.811

166

115.0

2256.74

225.7

6.79

–

–

–

0.875

18.250

261.587

52.573

5.24

4.778

179

113.4

2408.69

240.9

6.77

80

–

–

1.031

17.938

252.719

61.440

5.24

4.696

209

109.6

2771.62

277.2

6.72

100

–

–

1.281

17.438

238.827

75.332

5.24

4.565

256

103.5

3315.02

331.5

6.63

120

–

–

1.500

17.000

226.980

87.179

5.24

4.451

296

98.40

3754.15

375.4

6.56

140

–

–

1.750

16.500

213.825

100.335

5.24

4.320

341

92.70

4215.62

421.6

6.48

160

–

–

1.968

16.064

202.674

111.486

5.24

4.206

379

87.87

4585.21

458.5

6.41

–

–

SS

0.188

21.624

367.250

12.883

5.76

5.661

43.8

159.2

766.190

69.65

7.71

–

–

10S

0.218

21.564

365.215

14.918

5.76

5.645

50.7

158.3

884.816

80.44

7.70

10

–

–

0.250

21.500

363.050

17.082

5.76

5.629

58.1

157.4

1010.26

91.84

7.69

20

Std

–

0.375

21.250

354.656

25.476

5.76

5.563

86.6

153.8

1489.67

135.4

7.65

30

XS

–

0.500

21.000

346.361

33.772

5.76

5.498

115

150.2

1952.45

177.5

7.60

22

–

–

–

0.625

20.750

338.163

41.970

5.76

5.432

143

146.6

2399.00

218.1

7.56

22.0000

–

–

–

0.750

20.500

330.064

50.069

5.76

5.367

170

143.1

2829.69

257.2

7.52

60

–

–

0.875

20.250

322.062

58.070

5.76

5.301

197

139.6

3244.91

295.0

7.48

80

–

–

1.125

19.750

306.354

73.778

5.76

5.171

251

132.8

4030.43

366.4

7.39

100

–

–

1.375

19.250

291.039

89.094

5.76

5.040

303

126.2

4758.50

432.6

7.31

120

–

–

1.625

18.750

276.117

104.016

5.76

4.909

354

119.7

5432.00

493.8

7.23

140

–

–

1.875

18.250

261.587

118.546

5.76

4.778

403

113.4

6053.72

550.3

7.15

160

–

–

2.125

17.750

247.450

132.683

5.76

4.647

451

107.3

6626.39

602.4

7.07

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79

P ROPERTIES

Nom. Pipe Size, O.D. Inches

24 24.0000

26 26.0000

28 28.0000

30 30.0000

32 32.0000

80

Schedule Number* a b c 10 20 – 30 – 40 – – – 60 80 100 120 140 160 – 10 – 20 – – – – – – 10 – 20 30 – – – – – 10 – 20 30 40 – – – – 10 – 20 30 40 – – – –

– – Std – XS – – – – – – – – – – 5S – – – – – – – – – – – – – – – – – – Std – XS – – – – – – – – – – – – – – – Std – XS – – – – – – – – – – – – 5S – 10S Std – XS – – – – – – – – – – – – – – – Std – XS – – – – – – – – – – – – –

Wall Inside Thickness Diameter Inch Inch 0.250 0.375 0.500 0.562 0.625 0.687 0.750 0.218 0.875 0.968 1.218 1.531 1.812 2.062 2.343 0.250 0.312 0.375 0.500 0.625 0.750 0.875 1.000 1.125 0.250 0.312 0.375 0.500 0.625 0.750 0.875 1.000 1.125 0.250 0.312 0.375 0.500 0.625 0.750 0.875 1.000 1.125 0.250 0.312 0.375 0.500 0.625 0.688 0.750 0.875 1.000 1.125

23.500 23.250 23.000 22.876 22.750 22.626 22.500 23.564 22.250 22.064 21.564 20.938 20.376 19.876 19.314 25.500 25.376 25.250 25.000 24.750 24.500 24.250 24.000 23.750 27.500 27.376 27.250 27.000 26.750 26.500 26.250 26.000 25.750 29.500 29.376 29.250 29.000 28.750 28.500 28.250 28.000 27.750 29.500 31.376 31.250 31.000 30.750 30.624 30.500 30.250 30.000 29.750

Inside Area Sq. In.

Metal Area Sq. In.

433.736 424.557 415.476 411.008 406.493 402.073 397.608 436.102 388.821 382.348 365.215 344.318 326.083 310.276 292.978 510.705 505.750 500.740 490.874 481.105 471.435 461.863 452.389 443.014 593.957 588.613 583.207 572.555 562.001 551.546 541.188 530.929 520.768 683.493 677.759 671.957 660.520 649.181 637.940 626.797 615.752 604.806 683.493 773.188 766.990 754.768 742.643 736.569 730.617 718.688 706.858 695.126

18.653 27.833 36.914 41.382 45.897 50.316 54.782 16.288 63.568 70.042 87.174 108.071 126.307 142.114 159.412 20.224 25.179 30.189 40.055 49.824 59.494 69.066 78.540 87.916 21.795 27.139 32.545 43.197 53.751 64.206 74.564 84.823 94.984 23.366 29.099 34.901 46.338 57.678 68.919 80.062 91.106 102.053 23.366 31.060 37.257 49.480 61.605 67.678 73.631 85.559 97.389 109.121

Weight Outside Inside Weight of Water Surface Surface per Foot per Foot Sq. Ft./Ft. Sq. Ft./Ft. Lbs.† Lbs. 6.28 6.28 6.28 6.28 6.28 6.28 6.28 6.28 6.28 6.28 6.28 6.28 6.28 6.28 6.28 6.81 6.81 6.81 6.81 6.81 6.81 6.81 6.81 6.81 7.33 7.33 7.33 7.33 7.33 7.33 7.33 7.33 7.33 7.85 7.85 7.85 7.85 7.85 7.85 7.85 7.85 7.85 7.85 8.38 8.38 8.38 8.38 8.38 8.38 8.38 8.38 8.38

Anvil International, Piping & Pipe Hanger Design and Engineering

6.152 6.087 6.021 5.989 5.956 5.923 5.890 6.169 5.825 5.776 5.645 5.482 5.334 5.204 5.056 6.676 6.643 6.610 6.545 6.480 6.414 6.349 6.283 6.218 7.199 7.167 7.134 7.069 7.003 6.938 6.872 6.807 6.741 7.723 7.691 7.658 7.592 7.527 7.461 7.396 7.330 7.265 7.723 8.214 8.181 8.116 8.050 8.017 7.985 7.919 7.854 7.789

63.4 94.6 125 141 156 171 186 55.4 216 238 296 367 429 483 542 68.8 85.6 103 136 169 202 235 267 299 74.1 92.3 111 147 183 218 253 288 323 79.4 98.9 119 158 196 234 272 310 347 79.4 106 127 168 209 230 250 291 331 371

188.0 184.1 180.1 178.2 176.2 174.3 172.4 189.1 168.6 165.8 158.3 149.3 141.4 134.5 127.0 221.4 219.3 217.1 212.8 208.6 204.4 200.2 196.1 192.1 257.5 255.2 252.8 248.2 243.6 239.1 234.6 230.2 225.8 296.3 293.8 291.3 286.4 281.4 276.6 271.7 267.0 262.2 296.3 335.2 332.5 327.2 322.0 319.3 316.8 311.6 306.5 301.4

Moment Section of Inertia Modulus In.4 In.3 1315.34 1942.30 2549.35 2843.20 3136.93 3421.28 3705.46 1151.59 4255.34 4652.61 5671.82 6851.69 7824.55 8625.01 9455.42 1676.38 2077.16 2478.42 3257.00 4012.56 4745.57 5456.48 6145.74 6813.80 2098.09 2601.02 3105.12 4084.81 5037.66 5964.16 6864.82 7740.10 8590.49 2585.18 3206.31 3829.44 5042.21 6224.01 7375.38 8496.84 9588.93 10652.1 2585.18 3898.89 4658.48 6138.62 7583.39 8298.32 8993.35 10369.1 11711.1 13020.0

109.6 161.9 212.4 236.9 261.4 285.1 308.8 95.97 354.6 387.7 472.7 571.0 652.0 718.8 788.0 129.0 159.8 190.6 250.5 308.7 365.0 419.7 472.7 524.1 149.9 185.8 221.8 291.8 359.8 426.0 490.3 552.9 613.6 172.3 213.8 255.3 336.1 414.9 491.7 566.5 639.3 710.1 172.3 243.7 291.2 383.7 474.0 518.6 562.1 648.1 731.9 813.7

OF

P IPE

Radius Gyration In. 8.40 8.35 8.31 8.29 8.27 8.25 8.22 8.41 8.18 8.15 8.07 7.96 7.87 7.79 7.70 9.10 9.08 9.06 9.02 8.97 8.93 8.89 8.85 8.80 9.81 9.79 9.77 9.72 9.68 9.64 9.60 9.55 9.51 10.52 10.50 10.47 10.43 10.39 10.34 10.30 10.26 10.22 10.52 11.20 11.18 11.14 11.09 11.07 11.05 11.01 10.97 10.92

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P ROPERTIES

Nom. Pipe Size, O.D. Inches

OF

Schedule Number* a b c

P IPE

Wall Inside Thickness Diameter Inch Inch

Inside Area Sq. In.

Metal Area Sq. In.

Weight Outside Inside Weight of Water Surface Surface per Foot per Foot Sq. Ft./Ft. Sq. Ft./Ft. Lbs.† Lbs.

Moment Section of Inertia Modulus In.4 In.3

Radius Gyration In.

–

–

–

0.250

33.500

881.413

26.507

8.90

8.770

90.1

382.1

3774.38

222.0

11.93

10

–

–

0.312

33.376

874.900

33.020

8.90

8.738

112

379.3

4684.65

275.6

11.91

–

Std

–

0.375

33.250

868.307

39.614

8.90

8.705

135

376.4

5599.28

329.4

11.89

20

XS

–

0.500

33.000

855.288

52.632

8.90

8.639

179

370.8

7384.89

434.4

11.85

34

30

–

–

0.625

32.750

842.389

65.532

8.90

8.574

223

365.2

9127.59

536.9

11.80

34.0000

40

–

–

0.688

32.624

835.919

72.001

8.90

8.541

245

362.4

9991.61

587.7

11.78

–

–

–

0.750

32.500

829.577

78.343

8.90

8.508

266

359.7

10832.2

637.2

11.76

–

–

–

0.875

32.250

816.863

91.057

8.90

8.443

310

354.1

12497.9

735.2

11.72

–

–

–

1.000

32.000

804.248

103.673

8.90

8.378

352

348.7

14125.4

830.9

11.67

–

–

–

1.125

31.750

791.730

116.190

8.90

8.312

395

343.2

15715.1

924.4

11.63

–

–

–

0.250

35.500

989.798

28.078

9.42

9.294

95.5

429.1

4485.90

249.2

12.64

10

–

–

0.312

35.376

982.895

34.981

9.42

9.261

119

426.1

5569.48

309.4

12.62

–

Std

–

0.375

35.250

975.906

41.970

9.42

9.228

143

423.1

6658.92

369.9

12.60

36

20

XS

–

0.500

35.000

962.113

55.763

9.42

9.163

190

417.1

8786.20

488.1

12.55

36.0000

30

–

–

0.625

34.750

948.417

69.459

9.42

9.098

236

411.2

10868.4

603.8

12.51

40

–

–

0.750

34.500

934.820

83.056

9.42

9.032

282

405.3

12906.1

717.0

12.47

–

–

–

0.875

34.250

921.321

96.555

9.42

8.967

328

399.4

14900.0

827.8

12.42

–

–

–

1.000

34.000

907.920

109.956

9.42

8.901

374

393.6

16850.7

936.2

12.38

–

–

–

1.125

33.750

894.618

123.258

9.42

8.836

419

387.9

18758.9

1042.2

12.34

–

–

–

0.250

41.500

1352.652

32.790

11.00

10.86

111

586.4

7144.71

340.2

14.76

–

Std

–

0.375

41.250

1336.404

49.038

11.00

10.80

167

579.4

10621.6

505.8

14.72

20

XS

–

0.500

41.000

1320.254

65.188

11.00

10.73

222

572.4

14035.8

668.4

14.67

42

30

–

–

0.625

40.750

1304.203

81.240

11.00

10.67

276

565.4

17388.1

828.0

14.63

42.0000

40

–

–

0.750

40.500

1288.249

97.193

11.00

10.60

330

558.5

20679.3

984.7

14.59

–

–

–

1.000

40.000

1256.637

128.805

11.00

10.47

438

544.8

27081.3

1289.6

14.50

–

–

–

1.250

39.500

1225.417

160.025

11.00

10.34

544

531.3

33247.7

1583.2

14.41

–

–

–

1.500

39.000

1194.591

190.852

11.00

10.21

649

517.9

39184.3

1865.9

14.33

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N OTES

82

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Order dOcument #010

Order dOcument #165

ANVIL INTERACTIVE CD Order dOcument #899 • Browse the latest Gruvlok catalog, Submittal Sheets, technical data, cAd drawings, Fire-rite™ training • Browse the Pipe Hanger catalog & Submittal Sheets • Browse the Pipe Fittings catalog • Packed with Anvil Literature 1. Power-Strut engineering catalog 2. Pipe Fitters Handbook 3. Gruvlok HVAc Piping Products 4. engineered Hangers 5. data Sheets 6. and many more... • General Information on design Services (with an example video) • More of what you need...

GRUVLOK CATALOG Order dOcument #040

ANVILSTAR FIRE PROTECTION BROCHURE Order dOcument #215

U.S. REGIONAL SERVICE CENTERS EASTERN REGION SERVICING: cOnnectIcut, deLAwAre, FLOrIdA, GeOrGIA, mAIne, mAryLAnd, mASSAcHuSettS, new HAmPSHIre, new JerSey, new yOrk, eASt PennSyLVAnIA, rHOde ISLAnd, VermOnt, VIrGInIA

800 malleable road columbia, PA 17512 tel: 708-534-1414 • Fax: 708-534-5441 toll Free: 1-800-301-2701 NORTHERN REGION SERVICING: ILLInOIS, IndIAnA, IOwA, kentucky, mIcHIGAn, mInneSOtA, neBrASkA, nOrtH And SOutH dAkOtA, OHIO, weSt PennSyLVAnIA, weSt VIrGInIA, wIScOnSIn

750 central Avenue university Park, IL 60466 tel: 708-534-1414 • Fax: 708-534-5441 toll Free: 1-800-301-2701 SOUTHERN REGION SERVICING: ALABAmA, ArkAnSAS, kAnSAS, LOuISIAnA, mISSISSIPPI, mISSOurI, OkLAHOmA, tenneSSee, texAS

1313 Avenue r Grand Prairie, tx 75050 tel: 972-343-9206 • Fax: 972-641-8946 toll Free: 1-800-451-4414 WESTERN REGION SERVICING: ALASkA, ArIzOnA, cALIFOrnIA, cOLOrAdO, HAwAII, IdAHO, mOntAnA, neVAdA, new mexIcO, OreGOn, utAH, wASHInGtOn, wyOmInG

1385 Greg Street Sparks, nV 89431 tel: 775-331-7029 • Fax: 775-331-5075 toll Free: 1-800-572-0051

INTERNATIONAL SALES CANADA Corporate Office Michael J. Warne, General manager 470 Seaman St. Stoney creek, Ontario L8e 2V9 tel: 905-664-1459 • Fax: 905-664-3190 EUROPE & MIDDLE EAST REGION Rick van Meesen, director of Sales the netherlands tel: +31 53 5725570 • Fax: +31 53 5725579 u.S. customer Service tel: 708-534-1414 • Fax: 708-534-5441 LATIN AMERICA u.S. customer Service tel: 708-534-1414 • Fax: 708-534-5441 PUERTO RICO r.r. Barril, Inc. tel: +1 787-982-1550 • Fax: +1 787-982-1570 u.S. customer Service tel: 708-534-1414 • Fax: 708-534-5441 MEXICO Jose Antonio Bueno mexico tel: +52 777 169 4546 u.S. customer Service tel: 708-534-1414 • Fax: 708-534-5441 #170 / Printed in uSA / 4.07 / 2.5m / © 2007 Anvil International, Inc.

Corporate Offices 110 corporate drive, Suite 10 • P.O. Box 3180 Portsmouth, nH 03802-3180 tel: 603-422-8000 • Fax: 603-422-8033 e-mail address — [email protected]

www.anvilintl.com

FOR SALES AND SERVICE INFORMATION CONTACT THE REGIONAL SERVICE CENTER NEAREST YOU OR VISIT OUR WEBSITE AT WWW.ANVILINTL.COM